MICROMACHINED FILTERS AND FLOW REGULATORS

Abstract: The fluid filters and fluid flow regulators are capable of accurately handling substantially continuous fluid flow rates as low as about 0.01 cc/day. The filters and flow regulators are so miniaturized, corrosion-resistant and non-toxic that they are suitable for being implanted in the human body; and are capable of being mass produced at costs so low, by using micromachining techniques, such as etching, that they may be considered to be disposable. The filters and flow regulators are passive devices which consume no electrical energy at all. The filters and flow regulators are reliable because they may have as few as only two parts, only one which is a moving part; and because they may handle fluids at very low pressures.

Description: MICROMACHINED FILTERS AND FLOW REGULATORS BACKGROUND OF THE INVENTION The present invention relates to fluid handling devices. More particularly, it relates to fluid filters and fluid flow regulators which are reliable, accurate, and capable of handling fluid flow rates which are so low that they may be measured in hundredths of a cubic centimeter per day; which may have a zero electrical energy consumption; and which may be economically mass produced by using micromachining processes. SUMMARY OF THE INVENTION In many medical situations, it is desirable to continually administer fluid medication to a patient over an extended period of time at a relatively low flow rate. Examples of such cases are the use of morphine for the treatment of malignant or non-malignant pain; the use of FUDR for cancer chemotherapy; and the use of baclofen for the treatment of intractable spasticity. This manner of administering the medication is desirable because the level of the fluid medication in the patient's blood remains at a relatively constant, medically effective level. By way of contrast, if the medication was administered periodically in larger doses, such as in tablet form by mouth, the level of the medication in the patient's blood may tend to fluctuate markedly over time, from too little to too much, rather than staying at the desired medically effective level. Accordingly, one general aspect of the present invention may be to provide filters and regulators which are capable of continually handling fluids over an extended period of time at relatively low flow rates, which may be as low as about 0.01 cc/day. In many medical situations it is desirable to have filters and regulators which are extremely small, so that they may be implanted within a patient's body. Accordingly, another general aspect of the present invention may be to provide filters and regulators which are so small that they may be easily implanted within a patient's body. However, when making filters and regulators which are so small, it becomes relatively easy to inadvertently clog any openings in the filters and regulators (such as its ports, channels, cavities, or gaps) if a bonding material is used to bond the various parts of the filters and regulators together. Accordingly, another general aspect of the present invention is to provide filters and regulators in which at least some of their parts are anodically bonded together, thereby eliminating the need to use a separate bonding material to bond those parts together. If the filters and regulators are intended to be implanted in a patient's body, it is preferable that they be passive devices, which do not consume any electrical energy at all. In medical situations, the reliability of the filters and regulators which handle the fluid medication must be very high. In general, reliability may be enhanced by simplifying the filters and regulators to have as few total parts as possible; to have as few moving parts as possible; and to have nominal operating pressures which are as low as possible. Accordingly, one general aspect of the present invention may be to provide filters and regulators which are inherently highly reliable because they may have a total of as few as two parts, as few as one of which may be a moving part. Another general aspect of the present invention may be to provide filters and regulators which may operate at relatively low pressures. In medical situations, it is desirable to have filters and regulators which have a fail-safe design so that if they are subjected to overpressures in excess of their nominal design limits, they are very resistant to failure, so that they do not deliver excessive amounts of the medication to the patient. Accordingly, another general aspect of the present invention may be to provide filters and regulators which, when subjected to an overpressure, may be resistant to being ruptured because their flexures or membranes may be at least partially supported by at least one other element of the filters and regulators; and which may reduce the flow of the medication, or shut it off altogether. In view of the generally high cost of medical care, it is desirable to provide high quality, accurate, reliable filters and regulators at a price which is so economical that the filters and regulators may be considered to be disposable. Accordingly, another general aspect of the present invention may be to achieve these goals by using micromachining processes to mass produce the filters and regulators, or parts thereof. Since many medications and body fluids are corrosive, particularly where the filters and regulators are used for an extended period of time, or are implanted in a human or an animal, it is important that the filters and regulators be corrosion-resistant. Accordingly, three further general aspects of the present invention may be to provide filters and regulators having a layer of one or more corrosion- resistant substances; to bond such a corrosion-resistant layer to the filters and regulators by using anodic bonding; and to automatically perform such anodic bonding of the corrosion-resistant layer at the time certain other parts of the filters and regulators are being anodically bonded together. In many medical situations, it may be desirable to maintain the flow rate of the liquid medication to a patient at a predetermined rate, despite any fluctuations (either increases or decreases) in the pressure of the supply of the medication. For example, if the supply of the medication comprises a reservoir in which the medication is pressurized with a gas, as the reservoir is emptied the gas expands, thereby reducing the pressure on the decreasing amount of medication remaining in the reservoir. Accordingly, in addition to one or more of the above general aspects of the present invention, a specific aspect of the present invention may be to provide flow regulators which will maintain the flow of the medication within predetermined parameters, despite fluctuations in the pressure of the medication which is received by the flow regulator, or fluctuations in the pressure at the medication outlet port. Such a flow regulator may comprise a substrate having fluid inlet means, a regulator seat, and fluid outlet means. The flow regulator may further comprise a flexure bonded to the substrate, and a regulator gap which is located between the flexure and the regulator seat. During use, both the fluid inlet means and the outer surface of the flexure may be exposed to a source of liquid medication under pressure. The medication will flow sequentially through the fluid inlet means, the regulator gap and the fluid outlet means. As the medication flows through the regulator gap, the height of the regulator gap will tend to decrease as the driving pressure difference across the regulator increases, and will tend to increase as the driving pressure difference across the regulator decreases. As a result, the regulator will tend to hold the flow rate of the medication constant, despite any fluctuations in the driving pressure difference of the medication across the flow regulator. Another specific aspect of the flow regulator of the present invention may be that its flow rate may be selectively increased or decreased by selectively increasing or decreasing the number, size, shape and length of its fluid inlet means. A further specific aspect of the flow regulator of the present invention may be that its characteristic flow rate verses its applied driving pressure difference response may be chosen by selectively adjusting the fluid flow resistances of the fluid inlet means and the regulator gap with respect to each other. Other specific aspects of the flow regulator of the present invention may be that it may be a radial flow regulator, in which at least a portion of its fluid inlet means extend at least substantially around its regulator seat's periphery; in which its flexure overlies its regulator seat and extends outwardly past its regulator seat's periphery; in which at least part of its fluid outlet means are located within its regulator seat; and in which the medication flows from its fluid inlet means radially inwardly across its regulator seat's top surface, from its regulator's periphery to its fluid outlet means. In many medical applications the fluid flow rates of the medication may be very low, such as from about 0.01 cc per day to about 10.00 cc per day. As a result, the fluid passages in the filters and regulators which are capable of dealing with such very low flow rates have dimensions which may be as small as one or two microns, or less. Thus, the potential exists for such very small fluid passages to be clogged by even very small particles in the medication. Accordingly, in addition to one or more of the above general aspects of the present invention, a specific aspect of the present invention may be to provide a fluid filter which will filter out from the medication particles which may have a size as small as about 0.02 micron, or less. A further specific aspect of the filter of the present invention may be to provide a filter comprising as few as two basic components, namely a substrate and a membrane. Another specific aspect of the filter of the present invention may be that the filter may share its substrate and membrane with at least one other fluid handling device, such as a regulator, wherein such other fluid handling device also comprises the same substrate and membrane, and may receive filtered medication from the filter through fluid passages defined between the same substrate and membrane. Further specific aspects of the filter of the present invention may be to provide a radial array filter having a ring-shaped radial array of filter slots which are manufactured in the substrate; wherein the membrane serves as the cover for the filter slots; and wherein another fluid handling device, such as a regulator, which is to receive the filtered medication from the radial array filter, is located concentrically within the ring-shaped radial array of filter slots. Another specific aspect of the radial array filter of the present invention may be that it further comprises a ring-shaped inlet cavity, for distributing the incoming medication substantially equally to all of the filter slots; and a ring-shaped outlet cavity, for collecting the filtered medication from the filter slots substantially equally. The inlet and outlet cavities may also serve to provide a relatively uniform pressure drop across all of the filter slots. A further specific aspect of the present invention may be to provide a slab filter comprising a filter element suspended over an outlet cavity in the substrate; and an inlet port in the membrane for permitting the medication to reach the filter element. Other specific aspects of the present invention may be to provide a slab filter in which the edges of the filter element may sandwiched between the substrate and the membrane; and which may have a filter element entrance through which the filter element may be inserted into place over the slab filter's outlet cavity. Although all of the forgoing comments regarding the filters and regulators of the present invention have been with reference to handling medicinal fluids in a medical context, it is understood that the filters and regulators of the present invention may also be used to handle any type of non-medicinal fluid, in both medical and non- medical contexts. In addition, although the filters and regulators which were mentioned above may be very small and may handle fluids at very low flow rates and at relatively low pressures, it is understood that, by applying scaling laws, the filters and regulators of the present invention may, in general, be scaled up to any desired size; to handle any desired fluid flow rate and pressure. Further, the term "fluid" is used in its broad sense, and includes both liquids and gasses. It should be understood that the foregoing summary of the present invention does not set forth all of its features, advantages, characteristics, structures, methods and/or processes; since these and further features, advantages, characteristics, structures, methods and/or processes of the present invention will be directly or inherently disclosed to those skilled in the art to which it pertains by the following, more detailed description of the present invention. BRIEF DESCRIPTION OF THE FIGURES Fig. 1 is a top elevational view of a micromachined radial flow regulator of the present invention; Fig. 2 is a cross-sectional view thereof, taken substantially along line 2 - 2 of Fig. 1; Fig. 3 is a graph depicting certain of the fluid flow characteristics thereof; Fig. 4 is a schematic diagram of some of the fluid characteristics thereof; Figs. 5 and 6 are graphs depicting certain further fluid flow characteristics thereof; Fig. 7 is a perspective view, partly in a cross- section taken substantially along line 7 - 7 of Fig. 8, of a micromachined linear flow regulator having a contoured regulator seat; Fig. 8 is a top elevational view thereof; Figs. 9 - 11 are top elevational views of three additional embodiments thereof; Fig. 12 is a top elevational view of the substrate of the micromachined radial array filter of the present invention; Fig. 13 is a cross-sectional view thereof, taken substantially along line 13 - 13 of Fig. 12; Fig. 14 is a top elevational view of the substrate of a first embodiment of the micromachined slab filter of the present invention; Fig. 15 is a cross-sectional view thereof, taken substantially along line 15 - 15 of Fig. 14; Fig. 16 is a cross-sectional view thereof, taken substantially along line 16 - 16 of Fig. 14; and Fig. 17 is a top elevational view of the substrate of a second embodiment of the micromachined slab filter of the present invention. DESCRIPTION OF THE PREFERRED EMBODIMENTS MICROMACHINED RADIAL FLOW REGULATOR 32 (FIGS. 1 - 6): STRUCTURE Turning now to Figs. 1 - 2, the micromachined radial flow regulator 32 of the present invention may be used to control the flow rate of a fluid medication 12 passing through it. The term "medication" is used in its broad sense throughout this document, and may be any fluid, whether or not the fluid is medicinal in nature; unless the context should indicate otherwise. Similarly, the term "fluid" is also used in its broad sense throughout this document, and may include both liquids and gasses; unless the context should indicate otherwise. The radial flow regulator 32 may comprise a substrate 34 and a membrane 36. The substrate 34 may have four radially oriented inlet channels 38, a ring-shaped inlet cavity 40, a ring-shaped regulator seat 42, a cylindrical outlet cavity 52, and a venturi-shaped outlet port 54. In Fig. 1, the membrane 36 is depicted as being transparent, for clarity, so that the substrate 34's various features may be seen more easily. The membrane 36 may have four mounting portions 26, which are mounted to respective portions of the substrate 34's top surface 46; a circular, flexible flexure 28, which lies over the inlet cavity 40 and the regulator seat 42; and four inlet channel cover portions 30, each of which lie over a respective inlet channel 38. Although the membrane 36 is illustrated as being of uniform thickness, and as having flat bottom and top surfaces 50, 62, the membrane 36 may not be of uniform thickness, and may have bottom and top surfaces 50, 62 which are not flat. Although the membrane 36 is illustrated as having four mounting portions 26, it may have fewer or more mounting portions 26. A ring-shaped regulator gap 48 is provided between the regulator seat 42 and the flexure 28. Although four, straight, radially oriented inlet channels 38 are illustrated, each having a rectangular cross-sectional configuration and a respective cover portion 30, there may be fewer or more inlet channels 38, each having a respective cover portion 30; any particular inlet channel 38 may have any other suitable size and cross-sectional configuration, such as square or rounded; the length of any particular inlet channel 38 may be varied; and any particular radial inlet channel 38 need not follow a straight, radially oriented course, but may follow a circular, spiral, serpentine, or other non-straight, non- radially oriented course, such as do the channels 86 of the regulators 80 of Figs. 9 - 11. The use of one or more inlet channels 38 following a circular, spiral, serpentine, or other non-straight, non-radially oriented course may be desirable since it may permit the manufacture of a radial flow regulator 32 which is more compact, as compared to a radial flow regulator 32 having straight, radially oriented inlet channels 38. Although the ring-shaped inlet cavity 40 is illustrated as having a circular or cylindrical configuration, and a uniform depth, it may have any other suitable size and configuration, and a non-uniform depth. In addition, although the inlet channels 38 and the inlet cavity 40 are illustrated as being separate elements, it is understood that these elements may be merged into each other so that they are no longer distinct elements. This may be done in any suitable way, such as by enlarging the inlet channels 38 until they perform most, if not all, of the functions of the inlet cavity 40; by enlarging the inlet cavity 40 until it performs most, if not all, of the functions of the inlet channels 38; or by any combination of the forgoing two ways. Although the ring-shaped regulator seat 42 is illustrated as having a circular or cylindrical configuration, a flat top surface 44, and a uniform thickness, it may have any other suitable size and configuration, a top surface 44 which is not flat, and a non-uniform thickness. Although the ring-shaped regulator gap 48 is illustrated as having a circular or cylindrical configuration, and a uniform height, it may have any other suitable size and configuration, and a non-uniform height. Although the regulator gap 48 is illustrated as being formed by selecting the regulator seat 42 to have a thickness such that its top surface 44 is lower than the portions of the substrate 34's top surface 46 to which the membrane 36's mounting portions 26 are secured, the regulator gap 48 may be formed in any other suitable way. For example, the regulator seat 42's top surface 44 and the substrate 34*s top surface 46 may be selected to be co- planar, and the regulator gap 48 may be formed by reducing the thickness of the portion of the flexure 28 which overlies the regulator 42 by an amount equal to the desired height of the regulator gap 48. Alternatively, the regulator gap 48 may be formed by a combination of the two forgoing ways. Although a single outlet cavity 52, and a single outlet port 54 are illustrated, there may be more than one of each of these elements. Although an outlet cavity 52 having a circular or cylindrical configuration and a uniform depth is illustrated, it may have any other suitable size and configuration, and a non-uniform depth. The outlet cavity 52 may be used to define a clean outer perimeter for the outlet port 54, particularly if the outlet port 54 is drilled with a laser. However, the outlet cavity 52 may be eliminated, and the outlet port 54 may be extended upwardly so that it communicates directly with the regulator gap 48. Alternatively, the outlet port 54 may be eliminated, and the outlet cavity 52 may be extended downwardly so that it communicates directly with the regulator 32's bottom surface 56. Although an outlet port 54 having a venturi-shaped configuration is illustrated, it may have any other suitable configuration, such as round or cylindrical. Although the inlet cavity 40, the regulator seat 42, the regulator gap 48, the outlet cavity 52 and the outlet port 54 are illustrated as being uniformly arranged with respect to each other around a common center, they may be arranged with respect to each other in any other suitable way, and may not have a common center. The regulator 32 may have a flow rate for medical applications in the range of from about 0.01 cc/day to about 20 cc/day; and preferably in the range of from about 0.1 cc/day to about 2.0 cc/day. However, it is understood that, in view of all of the disclosures contained in this document, the radial flow regulator 32 may be scaled up or down in size to regulate higher or lower flow rates of the medication 12. By way of example, the chip bearing the radial flow regulator 32 may be a square having sides about 4.83 mm long. Its membrane 36 may be manufactured from silicon; and may have a thickness of about 25 microns. Its substrate 34 may have a thickness of about 0.5 mm, and may be manufactured from 7740 Pyrex glass, manufactured by the Corning Company located in Corning New York. The inlet channels 38 may have a length of about 2.54 mm, a width of about 107 microns, and a depth of about 5.65 microns. The ring-shaped inlet cavity 40 may have a depth of about 5.65 microns, an O.D. (outer diameter) of about 2.29 mm, and an I.D. (inner diameter) of about 1.52 mm, (i.e., the ring- shaped cavity 40 may have a radial width of about 0.77 mm). The ring-shaped regulator seat 42 may have an O.D. of about 1.52 mm and an I.D. of about 0.5 mm, (i.e. the ring-shaped regulator seat 42 may have a radial width of about 1.02 mm) . The ring-shaped regulator gap 48 may have a height of about 2.5 microns, when the driving pressure difference (P) across the flexure 28 is zero; and may have a radial width of about 1.02 mm. The outlet cavity 52 have a width of 0.5 mm, and a depth of about 3.15 microns. The outlet port 54 may have a minimum diameter of about 100 microns, and a depth of about 494 microns. The flow characteristics of this example radial flow regulator 32 are illustrated in Figs. 5 and 6. As will be appreciated from all of the disclosures in this document, the fact that the regulator 32 may, as in the example set forth above, have an extremely small size, be extremely light weight, have only two parts, and have a zero electrical energy consumption, offer numerous advantages over a regulator 32 which was physically much larger, much heavier, more complex or consumed electrical energy. For example, the regulator 32 may be ideal for use as part of a miniaturized medication delivery device which is to be implanted in a human or animal for delivery of constant flows of the medication 12 at flow rates as low as about 0.01 cc/day — flow rates which are so low that they may be impossible for a physically larger flow regulator of a different design to reliably and accurately deliver. MICROMACHINED RADIAL FLOW REGULATOR 32 (FIGS. 1 - 6) : OPERATION AND DESIGN The radial flow regulator 32 may be installed in its intended location of use in any suitable way. Any suitable medication supply means may be used to connect the radial flow regulator 32*s inlet channels 38 to a source of the medication 12; and any suitable medication delivery means may be used to connect the radial flow regulator 32's outlet port 54 to whatever person, animal or thing is to receive the medication 12 from the outlet port 54. In some cases, the medication supply means may also be used to supply the medication 12 to the flexure 28's top surface 62, at a pressure which may or may not be the same as the pressure at which the medication 12 is supplied to the inlet channels 38. For example, the radial flow regulator 32 may be installed within any type of reservoir means for the medication 12 by any suitable means, such as by locating the radial flow regulator 32*s outlet port 54 over the reservoir means's outlet, and by using an adhesive face seal between the radial flow regulator 32's bottom surface 56 and the inside of the reservoir means to hold the radial flow regulator 32 in place. As a result, when the reservoir means is filled with the medication 12, the radial flow regulator 32 will be immersed in the medication 12, with its inlet channels 38 and its flexure 28's top surface 62 in fluid communication with the medication 12 within the reservoir means, and with its outlet port 54 in fluid communication with the reservoir means' outlet. Such an installation for the radial flow regulator 32 has numerous advantages. For example, it is quick, easy, reliable and inexpensive, because no additional medication supply means (such as supply conduits) are needed to supply the medication 12 to the radial flow regulator 32's inlet channels 38 and to the flexure 28's top surface 62 (since they are already immersed in the medication 12) ; and because no additional medication delivery means (such as delivery conduits) are needed to convey the medication 12 away from radial flow regulator 32's outlet port 54 (since the reservoir means' outlet is used for this purpose). Such additional inlet and outlet conduits may be undesirable since it may be relatively time consuming, difficult and expensive to align and connect them to radial flow regulator 32, due to the extremely small size of its inlet channels 38, flexure 28, and outlet port 54. Such additional inlet conduits may also be undesirable because they may tend to trap a bubble when being filled with a liquid medication 12, which bubble might then be carried into the radial flow regulator 32 and cause it to malfunction. In the discussion which follows it will be assumed, for clarity and simplicity, that during operation of the radial flow regulator 32, the flexure 28's top surface 62 and the entrances of the inlet channels 38 are all exposed to a pressurized source of the medication 12 from the medication supply means. It will also be assumed, for clarity and simplicity, that the driving pressure difference (P) of the medication 12 across the radial flow regulator 32 is the pressure difference between the medication 12 at the membrane 36's top surface 62, and the medication 12 at the outlet port 54; which is the same as the pressure difference between the medication 12 at the entrances of the inlet channels 38 and the outlet port 54. However, it is understood that during operation of the radial flow regulator 23, these pressure differences need not be equal, and the flexure 28's top surface 62 does not necessarily have to be exposed to the pressurized source of the medication 12 from the medication supply means. When the flexure 28's top surface 62 is exposed to the medication 12, the driving pressure difference (P) across the flexure 28 may be the dominant factor in determining the amount of deflection of the flexure 28, and thus, the size of the regulator gap 48. On the other hand, if the flexure 28's top surface 62 is not exposed to the medication 12, then the velocity of the medication 12 through the regulator gap 48 may be the dominant factor in determining the amount of the deflection of the flexure 28, and thus, the size of the regulator gap 48. During operation, as a driving pressure difference (P) is applied across the radial flow regulator 32, such as by pressurizing the source of the medication 12 with respect to the radial flow regulator 32's outlet port 54 by any suitable means, the medication 12 will pass sequentially through the radial flow regulator 32's inlet channels 38, inlet cavity 40, regulator gap 48, outlet cavity 52, and outlet port 54. The inlet cavity 40 may serve to more or less equally distribute the flow of the medication 12 from the inlet channels 38 to the entire circumference of the regulator gap 48, for more predictable operation of the radial flow regulator 32. Referring now to Fig. 3, the regulator curves 64, 66, 68 and 70 are illustrated for a radial flow regulator 32 having one, two, three and four radial inlet channels 38, respectively. The triangular, diamond, circular and square data points on the regulator curves 64, 66, 68 and 70 are for the measured flow rate (Q) of an actual radial flow regulator 32 having the physical parameters of the example radial flow regulator 32 which was set forth above. The regulator curves 64, 66, 68 and 70, as well as all of the data points in Fig. 3, are plots of the flow rate (Q) of the medication 12 through the radial flow regulator 32 in microliters per day (μL/day) , as a function of the driving pressure difference (P) across the radial flow regulator 32 in millimeters of mercury (mm Hg) . As seen in Fig. 3, at a zero driving pressure difference (P) there is no flow of the medication 12 through the radial flow regulator 32, regardless of how many inlet channels 38 there may be. Then, as the driving pressure difference (P) is increased from zero, the radial flow regulator 32 exhibits four flow regimes, again regardless of the number of inlet channels 38 which it may have. That is, as the driving pressure difference (P) is increased from zero, there is a corresponding increase of the flow rate (Q) ; but there is also a gradual lessening of the flow rate's (Q's) sensitivity to the driving pressure difference (P) . For example, this is seen on the curve 66 from about a 0 mm Hg to about a 200 mm Hg driving pressure difference (P) . At intermediate driving pressure differences (P) there is a "control zone" wherein the flow rate (Q) is relatively insensitive changes in the driving pressure difference (P) . For example, this is seen on the curve 66 from mm Hg to about 300 mm Hg. Then, at driving pressure differences (P) higher than the "control zone", the flow rate (Q) actually decreases as the driving pressure difference (P) increases. For example, this is seen on the curve 66 from about 300 mm Hg to about 450 mm Hg. Finally, at very high driving pressure differences (P) , not illustrated in Fig. 3, the flow rate (Q) may gradually decrease to near zero as the driving pressure difference (P) of the medication 12 acting on the flexure 28's top surface 46 drives the flexure 28 down against the regulator seat 42. It has been discovered that the radial flow regulator 32 has a built-in, fail-safe characteristic, due to its structure, that may provide the user with exceptional protection against catastrophic failure of the flexure 28, when the flexure 28 is subjected to driving pressure differences (P) that are far in excess of the regulator 32's designed driving pressure difference (P) range. This fail-safe characteristic exists because, as has been mentioned, at very high driving pressure differences (P) the medication 12 acting on the flexure 28's top surface 46 may drive the flexure 28 down against the regulator seat 42's top surface 44. When this happens, the regulator seat 42 then acts as a support for the flexure 28 and prevents its further downward deflection; which further deflection might otherwise cause the flexure 28 to crack or rupture. As a result, a much higher driving pressure difference (P) is required to rupture the flexure 28 than would otherwise be the case, since the largest unsupported span of the flexure 28 is reduced in size from the maximum overall diameter of the inlet cavity 40, to the much smaller radial width of the ring-shaped inlet cavity 40. For example, for a flexure 28 which was a membrane of silicon about 25 microns thick, a driving pressure difference of at least about 100 psi (5,171 mm Hg) would be required to crack or rupture the flexure 28. By way of comparison, as seen in Fig. 3, the regulator 32's typical operating driving pressure difference (P) may be only about 300 mm Hg. Thus, in this instance, the regulator 32 would have about a 17 times overpressure safety factor. The type of response curves 64, 66, 68, 70 shown in Fig. 3 is highly desirable for many applications. This is because the radial flow regulator 32 will deliver a relatively constant flow rate (Q) of the medication 12 in its nominal "control zone", despite a substantial range of variations in the driving pressure difference (P) . In addition, if the nominal "control zone" driving pressure difference (P) is exceeded, then the flow rate (Q) of the medication 12 will not increase, but will actually decrease; thereby avoiding the possibility of damage which might otherwise be caused if the flow regulator 32 permitted more than the desired amount of the medication 12 to flow. For example, let us assume that a medication delivery device, having a source of medication 12 under pressure, was equipped with a radial flow regulator 32 in order to control the flow rate (Q) of the medication 12 from the medication delivery device. As a result, such a medication delivery device may be designed for operation in the radial flow regulator 32's above nominal "control zone" where the flow rate (Q) is relatively insensitive to changes in the driving pressure difference (P) . This may be highly desirable, since the patient will receive the medication 12 at the needed flow rate (Q) ; despite any variations in the driving pressure difference (P) , such as may be caused by the gradual emptying of the medication delivery device. In addition, if the nominal "control zone" driving pressure difference (P) were to be substantially exceeded, such as if a medical person accidentally overfilled the medication delivery device, then the medication flow rate (Q) will actually fall, thereby significantly reducing the possibility of injury or death to the patient, due to an overdose of medication 12, which might otherwise occur. The radial flow regulator 32 tends to maintain the flow rate (Q) of the medication 12 at a relatively constant value in its "control zone", despite changes in the driving pressure difference (P) , in the following way. If the driving pressure difference (P) increases, then the flexure 28 will tend to be deflected downwardly towards the regulator seat 42 an increased amount, thereby reducing the height of the regulator gap 48. This, in turn, tends to maintain the flow rate (Q) at a relatively constant value, despite the increased driving pressure difference (P) . This is because the reduced height of the regulator gap 48 will tend to compensate for the increased driving pressure difference (P) by reducing the flow rate (Q) which would otherwise occur at that increased driving pressure difference (P) . On the other hand, if the driving pressure difference (P) decreases, then the flexure 28 will tend to be deflected downwardly towards the regulator seat 42 a decreased amount, thereby increasing the height of the regulator gap 48. This, in turn, tends to maintain the flow rate (Q) at a relatively constant value, despite the reduced driving pressure difference (P) . This is because the increased height of the regulator gap 48 will tend to compensate for the reduced driving pressure difference (P) by increasing the flow rate (Q) which would otherwise occur at that reduced driving pressure difference (P) . Lastly, at driving pressure differences (P) above the regulator 32*s "control zone", the flow rate (Q) is gradually reduced to near zero, as the flexure 28 is driven down closer and closer to the regulator seat 42. Although the radial flow regulator 32 is deceptively simple in appearance, it has been discovered that it is not possible to develop simple, generally applicable design rules for its construction. This is in large part attributable to the close and nonlinear compensatory coupling between the flow rate (Q) through the radial flow regulator 32's regulator gap 48 and the flow resistance of the regulator gap 48 (R s ) ; which, in turn, makes it difficult to separate cause and effect in a mathematical sense. In addition, certain other problems arise in developing simple, generally applicable design rules for the radial flow regulator 32 because the flow rates (Q) of the medication 12 through the regulator 32 may be so low, (as low as about 0.01 cc per day), and because the dimensions of the inlet channels 38, the inlet cavity 40, the regulator gap 48, the outlet cavity 52 and the outlet port 54 may be so small, (as small as about 0.1 microns). As a result of such low flow rates (Q) and such small dimensions, certain fluid flow effects (such as the viscous shear forces of the medication 12 acting to deform various parts of the radial flow regulator 36) , which are normally negligible in predicting the performance of physically larger flow regulators, which handle flow rates of over about 0.1 cc per minute, for example, may become very important. In addition, certain other fluid flow effects (such as the Equation of Continuity and Bernoulli's Equation) , which are normally important for physically larger flow regulators, handling such higher flow rates (Q) , may become negligible for a regulator 32 having such low flow rates (Q) and such small dimensions. And, at intermediate flow rates (Q) and dimensions, a combination of the pertinent small scale and large scale fluid flow effects may have to be taken into account. Because of all of the above problems, it has been discovered that two quite different strategies may be used to assist in designing a radial flow regulator 32 which has any particular desired flow regulation characteristics. The first strategy is one which is empirical in nature. That is, a series of flow regulators 32 may be built, and one feature at a time may be varied, so that the effects of changing that particular feature may be determined. For example, the series flow resistance (R s ) of the regulator gap 48 may be independently varied by holding constant the regulator gap 48's initial height (when the driving pressure difference (P) is equal to zero) ; while varying the width of the ring-shaped regulator seat 42, such as by varying the I.D. and O.D. of the ring-shaped regulator seat 42. Similarly, the regulator gap 48's initial height (when the driving pressure difference (P) is equal to zero) may be varied; while holding constant the width of the ring shaped regulator seat 42, such as by holding constant the I.D. and O.D. of the ring-shaped regulator seat 42. By building and testing a large number of radial flow regulators 32; by then plotting data points for each of them for their various flow rates (Q) versus their driving pressure differences (P) ; and by then curve-fitting the plotted data points, it has been discovered that it is possible to generate an empirical model for the performance of the radial flow regulator 32 which shows the relationships between key features of the radial flow regulator 32 and the operating behavior of the radial flow regulator 32. These empirical relationships may then be used to interpolate or extrapolate from known design cases to predict the behavior of a new radial flow regulator 32. For example, it has been discovered that the radial flow regulator 32's flow rate set point (Q set ) (the average flow rate (Q) of the radial flow regulator 32 over its "control zone") obeys power-law relationships with respect to many of the radial flow regulator 32's design features. That is, it has been discovered that if the series flow resistance (R s ) of the regulator gap 48, and the regulator gap 48's initial height (when the driving pressure difference (P) is equal to zero) , are independently varied, then the radial flow regulator 32's flow rate set point (Q set ) may be described over a considerable range of values by an equation of the form: o = aGm Qset ~ Εξ where (Q set ) a nd (R s ) are as have been defined above; where (G) is the regulator gap 48's initial height (when the driving pressure difference (P) is equal to zero) ; and where (a) is a constant. For example, for a radial flow regulator 32 having a silicon flexure 28 with a thickness of about 25 microns; having channels 38 with a width of about 107 microns, with a depth of about 5.65 microns, and a length of about 2.54 mm; having a ring-shaped inlet cavity 40 with an O.D. of about 2,300 microns, and a depth of about 5.65 microns; having a ring-shaped regulator seat 42 with a width (as measured between its I.D. and O.D.) of about 750 - 2,000 microns; having an initial regulator gap 48 height (when the driving pressure difference (P) is equal to zero) in the range of about 2 - 3 microns; having an outlet cavity 52 about 5.65 microns deep; and having an outlet port 54 with a minimum diameter of about 100 microns and a length of about 494 microns, it has been discovered that (m) is on the order of about 2.4 and (n) is on the order of about 2/3. The second strategy which may be used to assist in designing a radial flow regulator 32 which has any particular desired flow regulation characteristics is to develop a sophisticated physical model using numerical methods. The starting point for formulating the model may be that, for any particular radial flow regulator 32, the flow of the medication 12 through it may be generally governed by the following equation: Q=- (R ch +R 3 (Q) ) where (Q) , (P) , and (R s ) are as has been defined above; where ( Ch ) is the combined flow resistance across the radial inlet channels 38; where ( Ch ) is a direct function of the length (L) and the wetted perimeter (C) of each of the radial inlet channels 38; where ( Ch ) s an inverse function of the cross-sectional area (A) of each of the radial inlet channels 38; and where (R s ) is a nonlinear function of the flow rate (Q) . That is, the flow rate (Q) is proportional to the driving pressure difference (P) , and is inversely proportional to the sum of the two flow resistances (R ch ) and (R s ) . A circuit diagram illustrating this behavior is shown in Fig. 4. It has been found that accurate prediction of the nonlinear flow resistance (R s ) of the regulator gap 48 may require the consideration of at least the following four factors. First, the nonlinear flow resistance (R s ) of the regulator gap 48 may be a function of the pressure drop across the inlet channels 38, due to their flow resistance (R ch ) . This is because the greater the pressure drop across the inlet channels 38, the greater the driving pressure difference (P) across the flexure 28, and the greater the amount of the deflection of the flexure 28 (and vice versa) . This, in turn, generally decreases the height of the regulator gap 48; thereby generally increasing the flow resistance (R s ) of the regulator gap 48 (and vice versa) . However, such deflection of the flexure 28 is not uniform, since the deflected flexure 28 is not flat, but instead assumes a convex, or bowed shape. This results in the nonlinear flow resistance (R s ) of the regulator gap 48 being a relatively complex function of the flow resistance (R ch ) of the inlet channels 38. Second, the nonlinear flow resistance (R s ) of the regulator gap 48 may be a function of the viscous shear forces of the medication 12 acting on the flexure 28's bottom surface 50 as the medication 12 flows radially inwardly through the regulator gap 40, from the inlet cavity 40 to the outlet cavity 52. Such viscous shear forces are, in turn, a function of such things as the viscosity and velocity of the medication 12 in the regulator gap 48. Such viscous shear forces are directed radially inwardly on the flexure 28's bottom surface 50, and tend to twist or distort the flexure 28's bottom surface 50 with respect to the flexure 28's top surface 62. Such twisting or distorting of the flexure 28 tends to vary the size and shape of the regulator gap 48 which, in turn, varies the flow resistance (R s ) of the regulator gap 48. This results in the nonlinear flow resistance (R s ) of the regulator gap 48 being a relatively complex function of the viscous shear forces of the medication 12 acting on the flexure 28. Third, the nonlinear flow resistance (R s ) may be a function of the velocity of the medication 12 passing through the regulator gap 48. Such velocity is, in turn, a function of such factors as the flow resistance (R ch ) of the inlet channels 38; the driving pressure difference (P) across the regulator 32; the height, size and shape of the regulator gap 48; and the flow resistance (R 8 ) of the regulator gap 48. Because of the Equation of Continuity and Bernoulli's Equation, as the velocity of the medication 12 through the regulator gap 48 increases, the pressure of the medication 12 within the regulator gap 48 tends to decrease (and vice versa) . This is because the Equation of Continuity requires that the velocity of the medication 12 must increase at a restriction. Thus, since the regulator gap 48 is a restriction (as compared to the inlet cavity 40) , the velocity of the medication 12 must increase as it flows through the regulator gap 48. Bernoulli's equation then requires that the pressure of the medication 12 in the regulator gap 48 must fall, due to its increased velocity as it flows through the regulator gap 48. That is, as the velocity of the medication 12 in the regulator gap 48 increases, the pressure of the medication 12 in the regulator gap 48 decreases. This increases the amount of the deflection of the flexure 28; which, in turn, generally decreases the height of the regulator gap 48 and increases the flow resistance (R s ) (and vice versa) . Fourth, the nonlinear flow resistance (R s ) may be a function of the flexure 28's thickness, resiliency, elasticity and stiffness. This is because for any given forces acting on the flexure 28, the amount of the deflection of the flexure 28, and the shape (or radial profile) of the deflected flexure 28, may be a function of the flexure 28's thickness, resiliency, elasticity and stiffness. In the forgoing discussion, it was assumed that the membrane 36's inlet channel cover portions 30 were selected such that they would not be deflected a substantial amount downwardly into the inlet channels 38 by the medication 12 during the operation of the radial flow regulator 32. Thus, the forgoing discussion assumed that substantially none of the regulation of the flow of the medication 12 by the flow regulator 32 was done by any such deflection of the 36's inlet channel cover portions 30. However, this need not be the case since, as will be made apparent by all of the disclosures in this document, regulation of the flow rate (Q) of the medication 12 through the radial flow regulator 32 may be at least partially done by such deflection of the membrane 36's inlet channel cover portions 30. From the forgoing, it is seen that the primary difficulty in developing a sophisticated physical model for the radial flow regulator 32 which uses numerical methods is that the amount of the deflection or bowing of the flexure 28, and the shape of the flexure 28 as it deflects or bows, are closely coupled and nonlinear in interaction. As a result, iterative techniques may be used to generate a solution for the flexure 28's deflected or bowed shape (a) that is correct at every point of contact between the medication 12 and the flexure 28 in terms of the forces applied to the flexure 28; and (b) that simultaneously provides a consistent radial gradient of the driving pressure difference (P) of the medication 12 across the flexure 28 which obeys the laws of fluid flow. To do this, a free body diagram may first be developed for an arbitrary ring-shaped segment of the flexure 28. This model creates the following governing fourth-order differential equation set that identifies the relationship between the flexure 28's local curvature and its thickness; Young's modulus and Poisson's ratio; and exterior forcing functions that include the shear between the medication 12 and the flexure 28, any driving pressure difference (P) across the flexure 28, and the flexure 28's radial tension. The governing fourth-order differential equation set may be determined in the following way. The first derivative of the deflection ( θ ) of the flexure 28 towards the regulator seat 42 is given by the following second order differential equation: Equation 1 where r is radial position with respect to the center of the flexure 28; ΔP(r) is the driving pressure difference across the flexure 28 at the radial position r; and D t is given by: D + =. Et' 'f 12(l-l 2 ) where E is Young's Modulus; t is the thickness of the flexure 28; and υ is Poisson's ratio. The actual deflection Y(r) of the flexure 28 is obtained by integrating above Equation 1: r Equation 2 where Y 0 is the centerline deflection of the flexure 28. Hence the governing differential equation set is fourth order. Next, a first-order differential equation may be developed for the flexure 28's driving pressure difference (P) pressure drop across the annular ring-shaped portion of the regulator gap 48 which is directly under the above mentioned arbitrary ring-shaped segment of the flexure 28. This differential equation must take into account not only the change in the regulator gap 48 caused by the amount of the deflection or bowing of the flexure 28, but also any change in the regulator gap 48 caused by the substrate 34's inlet channels 38 and inlet cavity 40. The first-order differential equation for the driving pressure difference ΔP(r) is: Equation 3 where ΔP-L is the driving pressure difference (P) at the outer rim of the inlet cavity 40, referenced to the constant pressure of the medication 12 external to the flexure 28; Q is the volumetric flow rate of the medication 12; μ is the viscosity of the medication 12; and H(r) is the height of the regulator gap 48 when the driving pressure difference (P) is equal to zero. In short, the above Equation 2 describes the amount and shape of the deflection or bowing of the flexure 28; while the above Equation 3 provides a means to calculate the driving pressure difference (P) of the medication 12 across the flexure 28 at any radial position with respect to the flexure 28. To be a physically correct representation of the interaction between the driving pressure difference (P) across the flexure 28, and the amount and shape of the deflection or bowing of the flexure 28, the solutions of the above Equations 2 and 3 must be consistent with each other in a point-to-point sense across the entire radius of the flexure 28. To achieve this goal, the above Equation 2 may be converted to a finite difference form, and a guess may be made as to the radial profile of the driving pressure difference (P) of the medication 12 across the flexure 28. This is necessary since a solution of the bowing or deflected flexure 28's above Equation 2 requires knowledge of the driving pressure difference (P) of the medication 12 across the flexure 28 at each radial position. This results in a so-called tridiagonal array of coupled equations that may be solved recursively for the flexure 28's radial slope at each point. Then this may be integrated once to yield the flexure 28's deflection at each radial position. Once this is known, the radial profile of the driving pressure difference (P) across the flexure 28 may be recalculated using these new deflection values for the flexure 28 by integration of the above Equation 3. The above iterative process may then be continued, as necessary, until the calculated position of the flexure 28 does not change by some arbitrarily set small amount per iteration, thereby signalling a consistent solution set. Any number of different cylindrically-symmetric fluid flow devices may be modeled with the above equation set. By changing the sign of Q, both inward and outward flow of the medication 12 through the devices may be modeled. By adjusting the function H(r) to reflect the height of the gap between the particular fluid flow device's flexure and the corresponding part of its substrate, the above equation set may be equally useful for modeling other flow regulators (such as the flow regulator 80) . Fig. 5 shows the above mathematical model being used to predict the response of a typical design for the flow regulator 32. The solid curve 72 in Fig. 5 shows a plot of the above mathematical model for the radial flow regulator 32, in terms of flow of the medication 12 through the regulator 32 in μL/day as a function of the driving pressure difference (P) across the flexure 28. The diamond-shaped data points 74 which are plotted in Fig. 5 are for a typical radial flow regulator 32 having a radial array of four rectangular inlet channels 38, each having a width of about 70 microns, a length of about 1270 microns, and a depth of about 5.7 microns; an inlet cavity having a maximum diameter of about 2290 microns, and a depth of about 5.7 microns; a regulator seat 42 having an I.D. of about 508 microns, and an O.D. of about 1780 microns; a flexure manufactured from a membrane of silicon having a thickness of about 25 microns; a regulator gap 48 having a height of about 2.5 microns (when the driving pressure difference (P) across the flexure 28 is zero) ; an outlet cavity having a diameter of about 508 microns, and a depth of about 5.7 microns; and an outlet port having a minimum diameter of about 100 microns, and a length of about 494 microns. The dashed curve 76 is an empirical curve which is derived by applying curve-fitting techniques to the plotted data points 74. As seen in Fig. 5, agreement between the theoretical curve 72 and the plotted data points 74 is very good. The curve 78 in Fig. 6 shows the above mathematical model being used to predict the reduction in the medication 12's flow rate setpoint (Q set ) caused by sealing off the four inlet channels 38 one-by-one. The diamond-shaped data points 74 which are plotted in Fig. 6 are for a typical radial flow regulator 32 having the physical parameters which were set forth above. As seen in Fig. 6, when one inlet channel 38 is sealed off, the effective combined flow resistance ( Ch ) of the remaining three channels 38 increases by about 33%, as compared to the combined flow resistance ( Ch ) of the original array of four inlet channels 38. Similarly, plugging two and three of the inlet channels 38 will increase the effective combined flow resistance (R ch ) of the remaining inlet channel(s) 38 by about 100% and about 400%, respectively. As seen in Fig. 6, the mathematical model curve 78 predicts this behavior of the radial flow regulator 32 very well. The qualitative effect of closing off one or more of the inlet channels 38 is to increase the driving pressure difference (P) across the flexure 28 which is needed for any given flow rate (Q) of the medication 12 through the radial flow regulator 32. This causes the flexure 28 to come into closer proximity to the regulator seat 42 at a lower flow rate (Q) , and hence biases the regulator 32's flow rate setpoint (Q set ) to a value for the flow rate (Q) which is lower than would otherwise be the case. It has been discovered that, as seen in Fig. 3, as the number of the inlet channels 38 is decreased, the "control zone" of the flow rate (Q) occurs at lower and lower flow rates (Q) for any given driving pressure difference (P) across the radial flow regulator 32. It has also been discovered that, as is also seen in Fig. 3, as the number of the inlet channels 38 is decreased, there may be a reduced sensitivity in the rate of change of the flow rate (Q) for any given change in the driving pressure difference (P) in the "control zone" of the flow rate (Q) . However, the theoretical grounds for this behavior of the regulator 32 are not clear, and it is possible that this behavior may be due to an artifact in a regulator 32 which is imperfect. All of the forgoing is very important, since it has been discovered that a single radial flow regulator 32 may actually have the properties of four different regulators 32, depending on whether none, one, two or three of its inlet channels 38 are sealed. That is, as seen in Fig. 3, such regulators 32 have quite different regulation curves 64, 66, 68, 70; have quite different "control zones" and flow rate set points (Q set ) ; have quite different flow rates (Q) for any given driving pressure difference (P) ; and have quite difference sensitivities to changes in their flow rates (Q) for any given change in the driving pressure difference (P) . This makes the present invention much more versatile, since a single radial flow regulator 32 may be easily modified to do the work of four single-function flow regulators. Of course, as was mentioned above, there may be fewer, or more, than four inlet channels 38; so one radial flow regulator 32 may be easily modified to do the work of fewer or more single-function flow regulators 32. From the disclosures in this document, it is possible to selectively design a radial flow regulator 32 for any particular desired flow regulation characteristics or driving pressure difference (P) . This may be done by selectively adjusting one or more of the pertinent parameters, such as: (a) the number, length, size, and cross sectional configuration of the radial inlet channels 38; (b) the number, size, cross-sectional configuration and location of the cavities 40, 52 and the outlet port 54; (c) the number, size, cross-sectional configuration and height of the regulator seat 42; (d) the number, size, cross- sectional configuration and height of the regulator gap 48; and (e) the thickness, resiliency, elasticity and stiffness of the membrane 36. For example, it has been discovered that by adjusting the fraction of the driving pressure difference (P) that is dropped across the radial inlet channels 38 in relation to the fraction of the driving pressure difference (P) which is dropped across the regulator gap 48 (by adjusting the flow resistance (R Ch ) °f the inlet channels 38 and the flow resistance (R s ) of the regulator gap 48 with respect to each other) , two things may be selectively modified. First, the degree of control of the regulator flow (Q) versus the driving pressure difference (P) may be selectively varied; and second, the amount of regulator flow (Q) versus the driving pressure difference (P) may also be selectively varied. MICROMACHINED RADIAL FLOW REGULATOR 32 (FIGS. 1 - 6) : MANUFACTURE The substrate 34 may be manufactured from any suitable strong, durable material which is compatible with the medication 12, and in which the inlet channels 38, the inlet cavity 40, the regulator seat 42, the outlet cavity 52, and the outlet port 54 may be manufactured in any suitable way, such as by using any suitable etching, molding, stamping and machining process. Such a machining process may include the use of physical tools, such as a drill; the use of electromagnetic energy, such as a laser; and the use of a water jet. The membrane 36 may be manufactured from any suitable strong, durable, flexible, material which is compatible with the medication 12. If the radial flow regulator 32 is intended to regulate a medication 12 which is to be supplied to a human or an animal, then any part of the regulator 32 which is exposed to the medication 12 should be manufactured from, and assembled or bonded with, non-toxic materials. Alternatively, any toxic material which is used to manufacture the regulator 32, and which is exposed to the medication 12 during use of the regulator 32, may be provided with any suitable non-toxic coating which is compatible with the medication 12. Suitable materials for the substrate 34 and the membrane 36 may be metals (such as titanium) , glasses, ceramics, plastics, polymers (such as polyimides) , elements (such as silicon) , various chemical compounds (such as sapphire, and mica) , and various composite materials. The substrate 34 and the membrane 36 may be assembled together in any suitable leak-proof way. Alternatively, the substrate 34 and the membrane 36 may be bonded together in any suitable leak-proof way, such as by anodically bonding them together; such as by fusing them together (as by the use of heat or ultrasonic welding) ; and such as by using any suitable bonding materials, such as adhesive, glue, epoxy, solvents, glass solder, and metal solder. Anodically bonding the substrate 34 and the membrane 36 together may be preferable for at least four reasons. First, anodic bonding is relatively, quick, easy and inexpensive. Second, an anodic bond provides a stable leak-proof bond. Third, since an anodic bond is an interfacial effect, there is no build-up of material at the bond; and the bond has essentially a zero thickness, which desirably creates no essentially no spacing between the substrate 34 and the membrane 36. As a result, an anodic bond does not interfere with the desired height of the regulator gap 32. Fourth, an anodic bond may be preferable since it eliminates the need for any separate bonding materials, which might otherwise clog or reduce the size of the inlet channels 38, the inlet cavity 40, the regulator seat 42, the regulator gap 48, the outlet cavity 52, and the outlet port 54; or which might lead to corrosion of the joint between the regulator 32's substrate 34 and membrane 36. One example of how the radial flow regulator 32 may be manufactured will now be given. The starting point may be a 76.2 mm diameter wafer of Corning 7740 Pyrex glass, which will form the regulator 32's substrate 34. The glass wafer may be cleaned in any suitable way, such as by immersing it in a buffered hydrofluoric acid (BHF) etchant for two minutes, rinsing it with distilled water, and drying it. A thin chrome metallization layer may then applied to the top surface of the glass wafer by any suitable means, such as with an electron beam evaporator. The chrome layer may provide a good adhesion surface for the subsequent application of photosensitive resist (photoresist) to the glass wafer's top surface. Following this, a thin layer of any suitable photoresist may be applied on top of the chrome layer, such as Microposit 1650 photoresist made by the Shipley Company, located in Newton, Massachusetts. The layer of photoresist may be dried in any suitable way, such as by baking it at about 90°C for about 25 minutes. An image of the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52 may then be exposed onto the photoresist in any suitable manner, such as by using a first mask and a mask aligner. This image may be developed (that is, the exposed photoresist may be removed) , by using any suitable photoresist developer, such as 351 developer, made by the above Shipley Company. The glass wafer may then be then rinsed in distilled water and dried. As a result of the forgoing procedure, the chrome layer will now bear an image, unprotected by the photoresist, of the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52. The unprotected portions of the chrome layer may then be removed by using any suitable chrome etch solution, such as Cyantek CR-7, made by the Cyantek Company, located in Fremont, California. The forgoing procedure will result in an image of the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52 having been formed on the top surface of the glass wafer, which image is unprotected by the layers of photoresist and chrome which cover the rest of the glass wafer's top surface. The image may then be etched into the glass wafer's top surface to any desired depth by any suitable means, such as by immersing the glass wafer's top surface in BHF etchant; rinsing the glass wafer in distilled water, and drying it. A suitable depth may be about 6.0 microns. Next, an image of the regulator seat 42 may then be exposed onto the photoresist on the glass wafer's top surface using a second mask. The newly exposed photoresist may then be developed; and the newly exposed portions of the chrome removed. Then the image of the regulator seat may be etched into the top surface of the glass wafer to any desired depth in any suitable manner, in order to define an elevation difference between the regulator seat 42's top surface 44 and the top surface of the glass wafer. A suitable elevation difference may be about 2.5 microns. At this point, it may be noted that the depths of the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52 will also have been automatically increased by about 2.5 microns, since they are also unprotected by the layers of chrome and photoresist. In other words, the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52 may intentionally be initially etched to a depth less than their desired final depth, in order to permit them to automatically and simultaneously reach their desired final depth while the regulator seat 42 was being etched. Note that the above procedure is unusually economical and quick, since if the four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52 were originally etched to their desired final depth, then the additional steps of re-coating the entire glass wafer with photoresist (in order to protect the etched four radial inlet channels 38, the inlet cavity 40, and the outlet cavity 52) , and then baking the photoresist, would have to be done prior to the exposing, developing and etching of the regulator seat 42. After the regulator seat 42 has been etched, the regulator 32's outlet port 54 may be formed by any suitable means, such as by drilling it with a focused beam from a 25W C0 2 laser, with a physical drill, or with a water jet drill. It has been discovered that when using a laser to form the outlet port 54, heating the glass wafer to near its anneal point improves the quality of the outlet port 54, and also reduces undesirable cracking of the glass wafer adjacent to the outlet port 54. Preferably, as seen in Fig. 2, the outlet port 54 may have a venturi-like shape, rather than being cylindrical in shape, for better fluid flow through it. It has also discovered that the outlet port 54 may be given its preferred venturi-like shape by drilling the outlet port 54 with a laser in the manner discussed above. The desired venturi-like shape may be automatically formed during the laser drilling process, and apparently results from the thermal effects of the laser beam interacting with the glass wafer as the outlet port 54 is being drilled through it with the laser beam. After the outlet port 54 has been drilled, the glass wafer may be lightly etched with BHF etchant, in order to remove any volatilized glass which may have condensed on the glass wafer adjacent to its outlet port 54. After the outlet port 54 has been formed, a nominal layer of one or more corrosion-resistant substances may be deposited onto the top surface of the glass wafer by any suitable means, such as by sputtering using an e-beam evaporator. As a result, the four radial inlet channels 38, the inlet cavity 40, the regulator seat 42, the outlet cavity 52, and the outlet port 54 will have been coated with a layer of the corrosion-resistant substance(s) . Suitable corrosion-resistant substances may be silicon, or may be metals, such as gold, platinum, chrome, titanium and zirconium, or may be the oxides of silicon or such metals. Such oxides may be formed by thermally oxidizing the corrosion-resistant substance(s) in air after it has been applied to the substrate 34. However, other suitable corrosion-resistant substances may be used, depending on the particular medication 12 with which the radial flow regulator 32 is designed to be used. The oxides of metals such as titanium and zirconium are well- known to be stable against water solutions over a wide pH range. The thickness of the layer of the corrosion- resistant substance(s) may be from 200 A - 1000 A; but the thickness may depend on the particular corrosion-resistant substance(s) being used, and on the particular medication 12 with which the radial flow regulator 32 is designed to be used. Alternatively, the layer of corrosion-resistant substance(S) may comprise a donut-shaped disk of such corrosion-resistant substance(s) , such as silicon, which may be bonded to the regulator seat 42's top surface 44 by any suitable means, such as by using any of the means which have been mentioned for bonding the substrate 34 and the membrane 36 together. Such a corrosion-resistant donut-shaped disk may be formed in any suitable way, such as by using a masking and etching process which is similar to that described above regarding the substrate 34. The starting point may be a clean epitaxial-coated silicon wafer, to which is applied a thin chrome metallization layer and a layer of photoresist. After the photoresist is dry, an image of the donut-shaped disk may then be exposed onto the photoresist. The exposed photoresist, and the underlying portions of the chrome layer, may then be removed, resulting in an image of the donut-shaped disk on the surface of the silicon wafer, which image is not protected by the photoresist or by the chrome layer. The exposed portions of the silicon wafer may then etched to a depth in excess of the desired thickness of the desired donut-shaped disk in any suitable way, such as by the use of an isotropic silicon etchant. For example, if a donut-shaped disk having a thickness of about 1 micron was desired, then the exposed portions of the silicon wafer may be etched to a depth of about 5 microns. The silicon wafer may then be cleaned; the etched faces of the silicon and glass wafers may then be aligned with each other, so that the donut-shaped disk on the silicon wafer is aligned with the regulator seat 42 on the glass wafer; and the silicon and glass wafers may then be bonded together in any suitable way, such as by using an anodic bonding process like that which will be described below regarding anodically bonding together the silicon and glass wafers that will form the regulator 32's substrate 34 and membrane 36. Next, the silicon wafer with the donut- shaped disk may then etched again in any suitable way, such as by the use of an anisotropic ethylene diamine etchant, until the desired ultimate thickness of the donut-shaped disk of silicon is obtained. The manufacture of only one substrate 34 and only one donut-shaped disk of corrosion-resistant material for the substrate 34's regulator seat 42 was described above. However, it will be appreciated that on any pair of glass and silicon wafers respective arrays of substrates 34 and corresponding donut-shaped disks of corrosion-resistant material may be manufactured simultaneously in a manner which is similar to that described above. If such is the case, the array of substrates 34 on the glass wafer may be aligned with, and then bonded to, the corresponding array of donut-shaped disks of corrosion-resistant material on the silicon wafer. After the final etching of the silicon wafer, the manufacture of each regulator 32 may then be completed in the manner which is set forth below. If a donut-shaped disk or layer of corrosion-resistant substance(s) is bonded or applied to the regulator seat 42, then the regulator seat 42 may have to be etched an additional amount during its above etching step prior to applying the donut-shaped disk or layer of corrosion- resistant substance(s) to the regulator seat 42's top surface 44. The additional amount of etching may be equal to the thickness of the donut-shaped disk or layer, in order to end up with the desired elevation difference between the regulator seat 42's top surface 44 and the top surface of the glass wafer (which will form the substrate 34) . It has been discovered that the donut-shaped disk or layer of corrosion-resistant substance(s) on the regulator seat 42's top surface 44 may serve an unexpected further function in addition to its corrosion-resistant function. That is, it may also prevent the regulator 32's membrane 36 from being inadvertently bonded to the regulator seat 42's top surface 44 when the membrane 36 is being bonded to the glass wafer, such as when the membrane 36 is being anodically bonded in the manner which will be described below. After the regulator seat 42 has been etched, and after any desired layer or disk of corrosion-resistant substance(s) has been applied to etched portions of the glass wafer, the photoresist and chrome which remain on the unetched portions of the glass wafer may be removed by any suitable means, such as by using standard lift-off techniques. Fabricating the membrane 36 and mounting it to the glass wafer (which is the substrate 34) , may be done in any suitable way. One suitable way is to start with a prime silicon wafer having a boron-doped epitaxial silicon layer which has been deposited onto its top surface. Since the boron doped epitaxial silicon layer will ultimately form the regulator 32's membrane 36, the layer's thickness will depend on the desired thickness of the membrane 36. The boron-doped epitaxial silicon layer, and thus the membrane 36, may be from 1 - 50 microns thick, for example. The boron doping may be in excess of 3 X 10 19 atoms of boron per cubic centimeter, which conveys a dramatic etch- resistance to the epitaxial silicon layer in silicon etchants based on ethylene diamine. The glass and silicon wafers may then be cleaned; dried; and anodically bonded together. The anodic bonding may be performed in any suitable way, such as by placing the respective top surfaces of the glass and silicon wafers in contact with each other in a vacuum chamber in an oven maintained at a temperature of about 500°C. A DC voltage of approximately 1000 volts may then be applied to the two wafers for a period of about 15 minutes, with the silicon wafer at a positive potential relative to the bottom surface of the glass wafer. An exponentially decaying current will flow through the wafers over this time period, at the end of which the two wafers will have been anodically bonded together, i.e., they will have been hermetically bonded to each other to form a silicon/glass sandwich. It has also been discovered that the anodic bonding process may also ensure that any corrosion- resistant substance(s) which were applied to the etched surfaces of the glass wafer are firmly attached to it. Upon cool-down, after the anodic bonding process is complete, the silicon wafer portion of the anodically bonded silicon/glass sandwich may be ground down; but preferably, the silicon wafer is not ground down so much that any of its boron doped epitaxial silicon layer is removed. For example, if the boron doped epitaxial silicon layer is from about 1 - 50 microns in thickness, then the silicon wafer portion of the bonded silicon/glass wafer sandwich may be ground down to about 125 microns in thickness. The remaining non-doped silicon in the silicon wafer may then be removed in any suitable way, such as by placing the ground down silicon/glass sandwich in an ethylene diamine etchant maintained at 112°C for 3.5 to 4.0 hours. A suitable ethylene diamine etchant may be PSE-300, manufactured by the Transene Corp. located in Rowley, Massachusetts. At the end of this time, the boron doped epitaxial silicon layer will be exposed in the form of a continuous, flat membrane 36 which is anodically bonded to the glass wafer (the substrate 34) , thereby forming the completed radial flow regulator 32, which is then cleaned and dried. The purpose of the above grinding step is simply to reduce the amount of silicon which needs to be etched away. Accordingly, as alternatives, the grinding step may be eliminated, with all of the undesired silicon being etched away; or a thinner silicon wafer may be used, so that there is less undesired silicon to begin with. The manufacture of only one radial flow regulator 32 was described above. However, it will be appreciated that on any pair of glass and silicon wafers numerous regulators 32 could be manufactured simultaneously in a manner similar to that described above. If such is the case, an array of substrates 34 may be simultaneously etched in the glass wafer before the silicon and glass wafers are aligned and bonded together. Then, all of the membranes 36 may be formed simultaneously by grinding and etching the silicon wafer to its desired final thickness. The silicon/glass sandwich may then be divided by any suitable means (such as dicing) into individual chips, each chip bearing at least one radial flow regulator 32. One of the advantages of using the etching and anodic bonding process which was described in detail above is that such a process enables high quality, very reliable radial flow regulators 32 to be mass produced in great numbers at a cost so low that the regulator 32 may be considered to be disposable. In addition, it should also be noted that the regulator 32 is stunning in its simplicity since it may have as few as only two parts (the substrate 34 and the membrane 36) ; and since it may have only one moving part (the membrane 36's flexure 28). Further, because the raw materials from which the regulator 32 may be manufactured may be very inexpensive, such as glass and silicon, the cost of the regulator 32 may held to a very low level. MICROMACHINED LINEAR FLOW REGULATOR 80 HAVING A CONTOURED REGULATOR SEAT 90 (FIGS. 7 - 11): MANUFACTURE The substrate 82 may be made from any suitable strong, durable material which is compatible with the medication 12, and in which the channel 86 and the outlet port 54 may be manufactured in any suitable way, such as by using any suitable etching, molding, stamping and machining process. Such a machining process may include the use of physical tools, such as a drill; the use of electromagnetic energy, such as a laser; and the use of a water jet. The membrane 84 may be made from any suitable strong, durable, flexible, material which is compatible with the medication 12. The membrane 84 may also be elastic. If the regulator 80 is intended to regulate a medication 12 which is to be supplied to a human or an animal, then any part of the regulator 80 which is exposed to the medication 12 should be made from, and assembled or bonded with, non-toxic materials. Alternatively, any toxic material which is used to manufacture the regulator 80, and which is exposed to the medication 12 during use of the regulator 80, may be provided with any suitable non-toxic coating which is compatible with the medication 12. Suitable materials for the substrate 82 and the membrane 84 may be metals (such as titanium) , glasses, ceramics, plastics, polymers (such as polyimides) , elements (such as silicon) , various chemical compounds (such as sapphire, and mica) , and various composite materials. The substrate 82 and the membrane 84 may be assembled together in any suitable leak-proof way. Alternatively, the substrate 82 and the membrane 84 may be bonded together in any suitable leak-proof way, such as by anodically bonding them together; such as by fusing them together (as by the use of heat or ultrasonic welding) ; and such as by using any suitable bonding materials, such as adhesive, glue, epoxy, glass solder, and metal solder. Anodically bonding the substrate 82 to the membrane 84 may be preferable for at least four reasons. First, anodic bonding is relatively, quick, easy and inexpensive. Second, an anodic bond provides a stable, leak-proof bond. Third, since an anodic bond is an interfacial effect, there is no build-up of material at the bond; and the bond has essentially a zero thickness, which desirably creates no essentially no spacing between the substrate 82 and the membrane 84. As a result, an anodic bond does not interfere with the desired height or shape of the regulator gap 99. Fourth, an anodic bond may be preferable since it eliminates the need for any separate bonding materials, which might otherwise clog or reduce the size of the inlet port 88, the channel 86, the regulator gap 99, and the outlet port 92; or which might lead to corrosion of the joint between the substrate 82 and the membrane 84. One example of how the linear flow regulator 80 may be manufactured will now be given. The starting point may be a 76.2 mm diameter wafer of Corning 7740 Pyrex glass, which will form the regulator 80's substrate 82. The channel 86 and its regulator seat 90 may then be formed in the substrate 82 in any suitable way. One suitable way may be to first etch a generally rectangular channel into the substrate 82, wherein the rectangular channel has a length and a depth about equal to the length and the depth of the desired channel 86 and regulator seat 90. The rectangular channel may be etched into the substrate 82 in any suitable way, such as by using a process which is the same as, or at least similar to, that used to etch the radial flow regulator 32's inlet channels 38 into its substrate 34. After the rectangular channel has been etched, the regulator 80's outlet port 92 may be formed. The structure, operation, theory and manufacture of the linear flow regulator 80's outlet port 92 is the same as, or at least similar to, that of the radial flow regulator 32's outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. After the outlet port 92 has been formed, a nominal layer of one or more corrosion-resistant substances may be deposited onto the top surface of the glass wafer in any suitable way. As a result, the channel 86, the regulator seat 90, and the outlet port 92 will have been coated with a layer of the corrosion-resistant substance(s) . The structure, operation, theory and manufacture of such a layer of one or more corrosion-resistant substances for the linear flow regulator 80 is the same as, or at least similar to, that of the radial flow regulator 32's layer of one or more corrosion-resistant substances, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. After the channel 86 and the regulator seat 90 have been etched, and after any desired layer of corrosion- resistant substance(s) has been applied to etched portions of the glass wafer, the photoresist and chrome which remain on the unetched portions of the glass wafer may be removed by any suitable means, such as by using standard lift-off techniques. At this point, certain work on the manufacture of the membrane 84 may be done before the desired channel 86 and regulator seat 90 may be completed. Manufacturing the membrane 84 and bonding it to the glass wafer (which is the substrate 82) may be done in any suitable way. The structure, operation, theory and manufacture of the linear flow regulator 80's membrane 84 and the bonding of the membrane 84 to its substrate 82 to form a silicon/glass sandwich is the same as, or at least similar to, the manufacture of the radial flow regulator 32's membrane 36, and the bonding of the membrane 36 to its substrate 34 to form a silicon/glass sandwich, except for those differences, which will be made apparent by an examination of all of the Figures and disclosures in this document. Some of those differences will now be addressed. It may be recalled that the starting point for the regulator 80*s membrane 84 may be a prime silicon wafer having a boron-doped epitaxial silicon layer which has been deposited onto one of its surfaces. Since the boron doped layer will ultimately form the regulator 80's membrane 84, the boron-doped layer's thickness will depend on the desired thickness of the membrane 84. The boron-doped layer has a dramatic etch-resistance to silicon etchants based on ethylene diamine; but is easily etched by isotropic etchants. The isotropic etchants will also easily etch the non-doped layer of the silicon wafer. Accordingly, the first step in manufacturing the regulator 80's membrane 84 is to first clean the silicon wafer; apply a thin chrome metallization layer to both of the wafer's surfaces; and then apply and dry a thin layer of any suitable photoresist on top of the chrome layer. An image of the inlet port 88 may then be exposed onto the photoresist on the silicon wafer's boron-doped layer, and then developed; after which the silicon wafer may be cleaned and dried. As a result of the forgoing procedure, the chrome layer over the boron-doped layer will now bear an image, unprotected by the photoresist, of the inlet port 88. The unprotected portion of the chrome layer may then be etched away; resulting in an image of the inlet port 88 having been formed on the boron-doped layer, which image is unprotected by the layers of photoresist and chrome which cover the rest of the silicon wafer. The image of the inlet port 88 may then be etched into the boron-doped layer to a depth which is at least slightly greater than the thickness of boron-doped layer in any suitable way, such as by using an isotropic etchant. The photoresist and the chrome layers may then be removed from the silicon wafer, which may then be cleaned and dried. The silicon and glass wafers may then be aligned, so that the etched image of the inlet port 88 in the boron- doped layer is in proper registry with the etched image of the channel 86 in the glass wafer. The etched surfaces of the silicon and glass wafers may then be anodically bonded together; after which the non-doped layer of the silicon wafer may then be etched and ground to produce the desired membrane 84, with the desired inlet port 88. The desired inlet port 88 is automatically formed during the etching and grinding of the non-doped layer of the silicon wafer because the isotropic etchant had previously completely etched away the image of the inlet port 88 in the boron- doped layer of the silicon wafer; so that when the non- doped layer of the silicon wafer is etched and ground away, the inlet port 88 is automatically formed. The desired contour may be imparted to the channel 86's regulator seat 90 in any suitable way. One suitable way may be to use a pressure forming method, in which the substrate 82 may first be placed into a forming device which restrains the substrate 82's bottom surface 104 and its lateral edges. A flat stencil having a cutout whose length and width corresponds to that of the desired channel 86 may be provided; the membrane 84 may be tightly sandwiched between the stencil and the substrate 82; and at least the substrate 82 may be heated to an elevated process temperature at which the substrate 82 is softened. For example, the elevated process temperature for a Pyrex glass substrate may be about 600°C. The portion of the membrane 84 which is exposed through the stencil (i.e., the flexure 98), may then exposed to a pressure about equal to the regulator 80's maximum designed driving pressure difference (P) , thereby deflecting the flexure 98 down into the softened substrate 82 and forming the channel 86's contoured regulator seat 90. For example, for a Pyrex glass substrate which is heated to about 600°C, the pressure may be about 100 pounds per square inch (psi) . The rectangular channel mentioned above, which was etched into the substrate 82, may aid in the formation of the desired contoured regulator seat 90 since all the deflected flexure 98 needs to do is to mold the rectangular channel's sides and bottom into the desired contour. The forming device for the substrate 82 may have a relief hole which permits the exit of any excess substrate 82 material which is displaced by the deflected membrane 84. Alternatively, the rectangular channel mentioned above may be dispensed with, and the flexure 98 may be deflected with pressure down into the softened substrate 82 to form the contoured regulator seat 90. The desired pressure may then be maintained on the flexure 98 while the substrate 82 is cooled and hardened, thereby forming the substrate 82's channel 86 with the desired contour in its regulator seat 90. The pressure may then be released, allowing the elastic flexure 98 to return to its undeflected configuration. The stencil, the forming device and any undesired displaced substrate 82 material may then be removed. Although the use of a heat softened substrate 82 was described above, the contoured regulator seat 90 may be pressure formed into the substrate 82 in any other suitable way. For example, the substrate 82 may be selected to be made from a material, such as an epoxy, a ceramic material or a solvent-softened material, which is soft at room temperature, and which is then hardened after the flexure 98 is deflected down into it by a chemical reaction, by the application of heat, or by the evaporation of the solvent, respectively. Another way to form the contoured regulator seat 90 may be to micromachine the desired contour into the substrate 82 by use of a laser beam. Such a laser beam may be regulated, by any suitable means, to have an intensity gradient similar to that of the desired contour of the channel 86's regulator seat 90, such as by projecting the laser beam through one or more suitable lenses and/or gradient filters. Another way of using a laser beam to micromachine the desired contour into the substrate 82 may be to project the laser beam through a mask to give at least a portion of the laser beam a cross-sectional configuration which is similar to that the desired contour of the regulator seat 90. The manufacture of only one linear flow regulator 80 was described above. However, it will be appreciated that on any pair of glass and silicon wafers numerous regulators 80 could be manufactured simultaneously in a manner similar to that described above. If such is the case, an array of substrates 82 may be simultaneously etched in the glass wafer before the silicon and glass wafers are aligned and bonded together. Then, all of the membranes 36, and their inlet ports 88 may be formed simultaneously. The silicon/glass sandwich may then be divided by any suitable means (such as dicing) into individual chips, each chip bearing at least one linear flow regulator 80. One of the advantages of using the etching, anodic bonding, and pressure forming process which was described in detail above is that such a process enables high quality, very reliable linear flow regulators 80 to be mass produced in great numbers at a cost so low that the regulator 80 may be considered to be disposable. In addition, it should also be noted that the regulator 80 is stunning in its simplicity since it may have as few as only two parts (the substrate 82 and the membrane 84) ; and since it may have only one moving part (the membrane 84's flexure 98) . Further, the cost of the regulator 80 may held to a very low level because the raw materials from which the regulator 80 may be made may be very inexpensive, such as glass and silicon. MICROMACHINED RADIAL ARRAY FILTER 340 (FIGS. 12 - 13): STRUCTURE The micromachined radial array filter 340 of the present invention is illustrated in Figs. 12 - 13 as having been manufactured with a radial flow regulator 32 on the same chip 342. The chip 342 may be disposable, in that it may discarded and replaced by a new chip 342 if the filter 340 becomes clogged with filtered particles from the medication 12, or if the regulator 32 does not function properly. Although the filter 340 and the regulator 32 are illustrated as having a geometric relationship in which the regulator 32 is nested inside of the filter 340, for an unusually compact and space-saving configuration; the filter 340 and the regulator 32 may have any other suitable geometric relationship with respect to each other on the chip 342; and the filter 340 and the regulator 32 may be located on separate chips. Although the filter 340 is described as being used in conjunction with a regulator 32, it may be used in conjunction with any other device, to supply filtered medication 12 to that device. For clarity, the corresponding parts of the regulator 32 of Figs. 12 - 13 have been given the same reference numerals as the regulator 32 of Figs. 1 - 2, since the regulator 32 of Figs. 12 - 13 has the same structure, operation, theory and manufacture as the regulator 32 of Figs. 1 - 2, except for those differences which will be made apparent by an examination of all of the Figures and all of the disclosures in this document. The filter 340 may comprise a substrate 34 and a membrane 36 which is secured to the substrate 34's top surface 46. The substrate 34 may have four inlet ports 344; an inlet cavity 346; a radial array of twenty-two filter slots 348, which alternate with twenty-two ribs 350; an outlet cavity 352; and four outlet ports 354. The membrane 36 may form the top surface of the inlet ports 344, the inlet cavity 346, the filter slots 348, the outlet cavity 352, and the outlet ports 354. Although four equally spaced inlet ports 344 are illustrated, each having a rectangular cross-sectional configuration and following an arcuate path, there may be fewer or more inlet ports 344, the inlet ports 344 may not be equally spaced, each inlet port 344 may have any other suitable size and shape, and each inlet port 344 may follow any other suitable path, whether or not that path is straight. The functions of each inlet port 344 may include transporting the medication 12 from a source of medication 12 to at least one inlet cavity 346. Although only a single inlet cavity 346 is illustrated, having a rectangular cross-sectional configuration, and following a ring-shaped path, there may be more than one inlet cavity 346, each communicating with at least one inlet port 344 and at least one filter slot 348, each inlet cavity 346 may have any other suitable size and shape, and each inlet cavity 346 may follow any other suitable path, whether or not that path is straight. The functions of each inlet cavity 346 may include transporting the medication 12 from at least one inlet port 344 to at least one filter slot 348. Although the inlet ports 344 and the inlet cavity 346 are illustrated as being discrete elements of the filter 340, they may be merged partially or wholly together, such as by enlarging the inlet ports 344 until they perform some or all of the functions of the inlet cavity 346, or by enlarging the inlet cavity 346 until it performs some or all of the functions of the inlet ports 344. Although a radial array of twenty-two identical filter slots 348 is illustrated, each filter slot 348 having a generally rectangular cross-sectional configuration, and a generally trapezoidal shape, the filter slots 348 may be arranged in any other suitable way or array with respect to each other, there may be fewer or more filter slots 348, each filter slot 348 may have any other suitable size, cross-sectional configuration, and shape, and all of the filter slots 348 need not be identical. The functions of the filter slots 348 may include removing undesired particles from the incoming medication 12; and guiding the medication 12 to the outlet cavity 352. Although a radial array of twenty-two ribs 350 is illustrated, each having a generally rectangular cross- sectional configuration and a generally trapezoidal shape, the ribs 350 may be arranged in any other suitable way or array with respect to each other, there may be fewer or more ribs 350, and each rib 350 may have any other suitable size, cross-sectional configuration, and shape. The functions of the ribs 350 may include helping to define the filter slots 348; and supporting the membrane 36. Although a only a single outlet cavity 352 is illustrated, having a square cross-sectional configuration, and following a ring-shaped path, there may be more than one outlet cavity 352, each communicating with at least one filter slot 348 and at least one outlet port 354, each outlet cavity 352 may have any other suitable size and shape, and each outlet cavity 352 may follow any other suitable path, whether or not that path is straight. The functions of each outlet cavity 352 may include transporting the medication 12 from at least one filter slot 348 to at least one outlet port 354. Although four equally spaced outlet ports 354 are illustrated, each having a rectangular cross-sectional configuration, and following a straight path, there may be fewer or more outlet ports 354, the outlet ports 354 may not be equally spaced, each outlet port 354 may have any other suitable size and shape, and each outlet port 354 may follow any other suitable path, whether or not that path is straight. The functions of each outlet port 354 may include transporting the medication 12 away from at least one outlet cavity 352, and delivering the medication 12 to whatever person, animal or thing may be receiving the medication 12 from the outlet port 354. Although the outlet ports 354 and the outlet cavity 352 are illustrated as being discrete elements of the filter 340, they may be merged partially or wholly together, such as by enlarging the outlet ports 354 until they perform some or all of the functions of the outlet cavity 352, or by enlarging the outlet cavity 352 until it performs some or all of the functions of the outlet ports 354. Although the outlet ports 354 are illustrated as forming the regulator 32's inlet ports 38, the outlet ports 354 and the inlet ports 38 may be discrete elements which may be fluidly connected in any suitable way by any suitable means. By way of example, the filter 340 may have the following physical parameters. The substrate 34 may be manufactured from 7740 Pyrex glass, may be a square having sides with a length of about 0.635 cm, and may have a maximum thickness of about 0.5 mm. Each inlet port 344 may have a width of about 0.5 mm, a depth of about 10 microns, and a length of about 250 microns. The inlet cavity 346 may have a width of about 0.0127 cm, a depth of about 10 microns, and an internal diameter of about 0.58 cm. There may be 22 filter slots 348 and 22 ribs 350, and the sides of each filter slot 348 and each rib 350 may lay on a respective radial ray emanating from the center of the filter 340. Each filter slot 348 may be about 0.10 to about 5.0 microns high. Each filter slot 348 and each rib 350 may lie between an inner circle having a diameter of about 0.33 cm, and an outer circle having a diameter of about 0.58 cm. The outlet cavity 352 may have a width of about 0.0254 cm, a depth of about 10 microns, and an outer diameter of 0.33 cm. Each outlet port 354 may have a depth of about 10 microns, a width of about 250 microns, and a length of about 250 microns. The membrane 36 may be manufactured from silicon and may have a thickness of about 25 microns. MICROMACHINED RADIAL ARRAY FILTER 340 (FIGS. 12 - 13): OPERATION AND THEORY The chip 342, with its filter 340 and regulator 32, may be installed in its desired location of intended use in any suitable way. Any suitable medication supply means may be used to connect the filter 340's inlet ports 344 to a source of the medication 12; and any suitable medication delivery means may be used to connect the regulator 32's outlet port 54 to whatever person, animal or thing is to receive the medication 12 from the outlet port 54. The medication supply means may also be used to supply the medication 12 to the flexure 28's top surface 62, at a pressure which may or may not be the same as the pressure at which the medication 12 is supplied to the inlet ports 344. For example, the chip 342 may be installed within any type of reservoir means for the medication 12 by any suitable means, such as by locating the regulator 32's outlet port 54 over the reservoir means's outlet, and by using an adhesive face seal between the substrate 34's bottom surface 56 and the inside of the reservoir means to hold the chip 342 in place. As a result, when the reservoir means is filled with the medication 12, the chip 342 will be immersed in the medication 12, with the filter 340's inlet ports 344 and the flexure 28's top surface 62 in fluid communication with the medication 12 within the reservoir means, and with the regulator 32's outlet port 54 in fluid communication with the reservoir means' outlet. Such an installation for the chip 342 has numerous advantages. For example, it is quick, easy, reliable and inexpensive, because no additional medication supply means (such as supply conduits) are needed to supply the medication 12 to the filter 340's inlet ports 344 and to the flexure 28's top surface 62 (since they are already immersed in the medication 12) ; and because no additional medication delivery means (such as delivery conduits) are needed to convey the medication 12 away from the regulator 32's outlet port 54 (since the reservoir means' outlet is used for this purpose) . Such additional inlet and outlet conduits may be undesirable since it may be relatively time consuming, difficult and expensive to align and connect them to the chip 342, due to the extremely small size of the filter 340's inlet ports 344, the flexure 28, and the regulator 32's outlet port 54. Such additional inlet conduits may also be undesirable because they may tend to trap a bubble when being filled with a liquid medication 12, which bubble might then be carried into the filter 340 and the regulator 32 and cause them to malfunction. Alternatively, if the chip 342 did not have a regulator 32, but had only a filter 340, then such a chip 342 may be installed in its intended location of use in any suitable way. Any suitable medication supply means may be used to connect the filter 340's inlet ports 344 to a source of the medication 12; and any suitable medication delivery means may be used to connect the filter 340*s outlet ports 354 to whatever person, animal or thing is to receive the medication 12 from the outlet ports 354. The driving pressure difference (P) across the filter 340 may be defined as the driving pressure difference (P) between the flexure 28*s top surface 62 and the outlet port 54. During operation, as a driving pressure difference (P) is applied across the filter 340 in any suitable way, such as by pressurizing the source of medication 12 with respect to the outlet port 54, the medication 12 will flow sequentially through the filter 340's inlet ports 344, inlet cavity 346, filter slots 348, outlet cavity 352, and outlet ports 354. From the filter 340's outlet ports 354, the medication 12 will then flow sequentially through the regulator 32 from its inlet ports 38 to its outlet port 54 in the manner which has been described previously regarding the regulator 32 of Figs. 1 - 2. The size of the filter 340's filter slots 348 is selected to be such that the filter slots 348 will be able trap the smallest particle which the filter 340 is designed to remove from the medication 12. The size of the filter slots 348 may depend on the size of the smallest particle which can be tolerated by the person, animal or thing which is to receive the filtered medication 12 from the filter 340. For example, if the filter 340 is intended to deliver the medication 12 to a regulator 32, as illustrated in Figs. 12 - 13, then preferably the filter 340's filter slots 348 may be chosen to have a size which is at least slightly smaller than the size of the smallest fluid path dimension in the regulator 32, namely its regulator gap 48. In this way, the filter slots 348 will be able to trap all of the particles in the medication 12 which might otherwise clog the smallest fluid path dimension in the regulator 32. It should be noted that the micromachining process for manufacturing the filter slots 348 in the substrate 34 may easily manufacture filter slots 348 which have a depth of from about 0.10 microns, or less, to about 10.00 microns, or greater. Any pressure exerted by the medication 12 on the membrane 36's top surface 62 may be prevented from reducing the desired height or cross-sectional configuration of the inlet ports 344, the inlet cavity 346, the filter slots 348, the outlet cavity 352 and the outlet ports 354 in any suitable way, such as by selectively adjusting one or more of the pertinent parameters, such as: (a) the stiffness, elasticity, resiliency, thickness, size, shape and cross- sectional configuration of the membrane 36; and (b) the length, width, size and shape of the inlet ports 344, the inlet cavity 346, the filter slots 348, the outlet cavity 352 and the outlet ports 354. For the longest, most effective life of the filter 340, it may be preferred that all of the filter slots 348 be utilized an approximately equal amount. This goal may be at least partially achieved in any suitable way, such as by selectively adjusting one or more of the pertinent parameters, such as: (a) selecting the cross-sectional area of the filter 340's inlet cavity 346 to be large enough so that the pressure drop of the medication 12 in the inlet cavity 346 between the adjacent inlet ports 344 may be reduced, or minimized, to the point that the flow of the medication 12 from the inlet ports 344 is distributed at least approximately equally by the inlet cavity 346 to each of the filter slots 348; (b) selecting the cross- sectional area of the filter 340's outlet cavity 352 to be large enough so that the pressure drop of the medication 12 in the outlet cavity 346 between adjacent outlet ports 354 may be reduced, or minimized, to the point that the outgoing flow of medication 12 is distributed at least approximately equally by the outlet cavity 352 to each of the outlet ports 354; and (c) selecting the cross-sectional areas of the filter 340's inlet cavity 346 and outlet cavity 352 so that the pressure drop of the medication 12 across each of the filter slots 348 may be at least approximately equal. The fluid resistance of the filter 340 to the medication 12 may be selectively adjusted in any suitable way, such as by selectively adjusting at least one of the pertinent parameters, such as the number, length, size, shape and path followed by the inlet ports 344, the inlet cavity 246, the outlet cavity 352, the outlet ports 354, and the filter slots 348. The filter 340 may be designed to have a small, or negligible, fluid flow resistance to the medication 12 when new, in order to provide a margin for an accumulation of filtered particles in the filter slots 348. That is, the filter 340 may be designed so that after a predetermined quantity of particles have been trapped by the filter slots 348, a predetermined minimum fluid flow rate (Q) of the medication 12, at a predetermined driving pressure difference (P) across the filter 340, will still be permitted to flow through the filter 340. If this is done, and if the filter 340 is used in conjunction with a regulator 32, such as is seen in Figs. 12 - 13, then any fluid flow resistance of the medication 12 within the regulator 32 which is needed for proper pressure bias of the flexure 28 may be provided by the regulator 32's inlet ports 38 and inlet cavity 40. Alternatively, the fluid flow resistance of the filter 340 may be selected to have a significant fluid flow resistance to the medication 12 when new, in order to provide for proper pressure bias of the regulator 32's flexure 28. In other words, such a filter 340 may provide the dual functions of: (a) filtering out undesired particles from the medication 12; and (b) defining the flow rate operating point of the regulator 32, i.e., defining the maximum flow rate (Q) of the medication 12 through the regulator 32. In this case, the flow rate (Q) of the medication 12 through the filter 340 may fall as its filter slots 348 become clogged with filtered particles during use, and it may be prudent to provide some level of medication pre-filtering. In general, it may be advantageous to provide the filter 340 with medication 12 which has been pre-filtered to a substantial degree to remove undesired particles from the medication 12 which are larger than the smallest particles which the filter 340 is intended to trap. By such pre-filtering of large particles from the medication 12, the useful life of the filter 340 may be greatly extended, since the filter 340 is a precision filter for filtering very small particles, and thus it may take only a relatively small number of large particles to clog it. MICROMACHINED RADIAL ARRAY FILTER 340 (FIGS. 12 - 13): MANUFACTURE The substrate 34 may be manufactured from any suitable strong, durable material which is compatible with the medication 12; in which the filter 340's inlet ports 346, inlet cavity 346, filter slots 358, outlet cavity 352 and outlet ports 354 may be manufactured in any suitable way; and in which the regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54 may be manufactured in any suitable way. Suitable ways may include using any suitable etching, molding, stamping and machining process. Such a machining process may include the use of physical tools, such as a drill; the use of electromagnetic energy, such as a laser; and the use of a water jet. The membrane 36 may be manufactured from any suitable strong, durable, flexible, material which is compatible with the medication 12. If the filter 340 and the regulator 32 are intended to regulate a medication 12 which is to be supplied to a human or an animal, then any part of the filter 340 and the regulator 32 which is exposed to the medication 12 should be manufactured from, and assembled or bonded with, non¬ toxic materials. Alternatively, any toxic material which is used to manufacture the filter 340 and the regulator 32, and which is exposed to the medication 12 during use of the filter 340 and the regulator 32, may be provided with any suitable non-toxic coating which is compatible with the medication 12. Suitable materials for the substrate 34 and the membrane 36 may be metals (such as titanium) , glasses, ceramics, plastics, polymers (such as polyimides) , elements (such as silicon) , various chemical compounds (such as sapphire, and mica) , and various composite materials. The substrate 34 and the membrane 36 may be assembled together in any suitable leak-proof way. Alternatively, the substrate 34 and the membrane 36 may be bonded together in any suitable leak-proof way, such as by anodically bonding them together; such as by fusing them together (as by the use of heat or ultrasonic welding) ; and such as by using any suitable bonding materials, such as adhesive, glue, epoxy, solvents, glass solder, and metal solder. Anodically bonding the substrate 34 and the membrane 36 together may be preferable for at least four reasons; which reasons were discussed previously regarding the regulator 32 of Figs. 1 - 2. One example of how the chip 342, with its filter 340 and regulator 32, may be manufactured will now be given. The starting point may be a 76.2 mm diameter wafer of Corning 7740 Pyrex glass, which will form the substrate 34. The filter 340's inlet ports 344, inlet cavity 346, filter slots 348, outlet cavity 352, and outlet ports 354; and the Figs. 12 - 13 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42 and outlet cavity 52 may be manufactured in the substrate 34 in any suitable way. One suitable way may be to use an etching process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42 and outlet cavity 52, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The Figs. 12 - 13 outlet port 54 may then be manufactured in the substrate 34 in any suitable way. One suitable way may be use a laser drilling process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. A layer of corrosion-resistant material(s) may then be applied to all of the surfaces of the filter 340's inlet ports 344, inlet cavity 346, filter slots 348, outlet cavity 352 and outlet ports 354; and to all of the surfaces of the Figs. 12 - 13 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54 in any suitable way. One suitable way may be to use an application process which is the same as, or at least similar to, that used to apply a layer of corrosion-resistant material(s) to the Figs. 1 - 2 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The Figs. 12 - 13 membrane 36 may be manufactured from a silicon wafer, and secured to the glass wafer (which is the Figs. 12 - 13 substrate 34) , in any suitable way. One suitable way may be to use a manufacturing and securing process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 membrane 36, and to secure it to the Figs. 1 - 2 substrate 34, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. As was mentioned above, although the filter 340 is illustrated in Figs. 12 - 13 as being manufactured on the chip 342 with a regulator 32, the filter 340 may be manufactured by itself on the chip 342, without a regulator 32. In such a case, all or part of the filter 340's outlet ports 354 may extend from the outlet cavity 352 down through the substrate 34 (in a fashion similar to the regulator 32's outlet port 54). Such downwardly extending outlet ports 354 for the filter 340 may have any suitable shape, such as a venturi shape; and may be manufactured in any suitable way. One suitable way may be use a laser drilling process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The manufacture of only one filter 340, and the manufacture of only one filter 340/regulator 32 combination were described above. However, it will be appreciated that on any pair of glass and silicon wafers the substrates 34 and the membranes 36 for a large number of filters 340, or filter 340/regulator 32 combinations could be manufactured simultaneously in a manner similar to that described above. If such is the case, an array of substrates 34 may be simultaneously etched in the glass wafer; their outlet ports 54 may be drilled, and the layer of one or more corrosion-resistant substances may be applied to the substrates 34. Then the silicon and glass wafers for the substrates 34 and the membranes 36 may be aligned and secured together. Then, all of the membranes 36 may be manufactured simultaneously by grinding and etching the silicon wafer to its desired final thickness. The silicon/glass substrate 34/membrane 36 sandwich may then be divided by any suitable means (such as dicing) into individual chips, each chip bearing at least one filter 340 or filter 340/regulator 32 combination. One of the advantages of using etching and andic bonding processes to manufacture the filter 340, .nd the filter 340/regulator 32 combination, is thar. su'- i processes enable high quality, very reliable filters 340, and filter 340/regulator 32 combinations, to be mass produced in great numbers at a cost so low that the filters 340 and the filter 340/regulator 32 combinations may be considered to be disposable. Further, it should also be noted that the filter 340 and the filter 340/regulator 32 combination are stunning in their simplicity since they both have only two basic parts, i.e. their substrates 34 and their membranes 36; and since the regulator 32 has only one moving part, i.e., its flexure 28, which merely bows during operation of the filter 340/regulator 32 combination. In addition, because the raw materials from which the filter 340 and the filter 340/regulator 32 combination may be manufactured may be very inexpensive, such as glass and silicon, the cost of the filter 340 and the filter 340/regulator 32 combination may held to a very low level. MICROMACHINED SLAB FILTER 380 (FIGS. 14 - 16): STRUCTURE The micromachined slab filter 380 of the present invention is illustrated in Figs. 14 - 16 as having been manufactured with a radial flow regulator 32 on the same chip 342. The chip 342 may be disposable, in that it may discarded and replaced by a new chip 342 if the filter 380 becomes clogged with filtered particles from the medication 12, or if the regulator 32 does not function properly. Although the filter 380 and the regulator 32 are illustrated as having a geometric relationship in which the filter 380 is along side of the regulator 32, the filter 380 and the regulator 32 may have any other suitable geometric relationship with respect to each other on the chip 342. For example, the filter 380 may be ring-shaped and sized so that the regulator 32 may be nested inside of the ring-shaped filter 380 (similar to the arrangement of the radial array filter 340 and the regulator 32 of Figs. 12 - 13) . Although the filer 380 and the regulator 32 are illustrated as being on the same chip 342, the filter 380 and the regulator 32 may be located on separate chips. Although the filter 380 is described as being used in conjunction with a regulator 32, it may be used in conjunction with any other device, to supply filtered medication 12 to that device. For clarity, the corresponding parts of the regulator 32 of Figs. 14 - 16 have been given the same reference numerals as the regulator 32 of Figs. 1 - 2, since the regulator 32 of Figs. 14 - 16 has the same structure, operation, theory and manufacture as the regulator 32 of Figs. 1 - 2, except for those differences which will be made apparent by an examination of all of the Figures and all of the disclosures in this document. The filter 380 may comprise a substrate 34; a filter element 390; and a membrane 36, which is secured to the substrate 34's top surface 46. The membrane 36 may have an inlet port 388. The substrate 34 may have a recessed filter mounting lip 382, for receiving the filter element 390's edges; an outlet cavity 384, which is at least partially surrounded by the recessed filter mounting lip 382; and a pair of outlet ports 386. Although only one, rectangular inlet port 388, filter mounting lip 382, filter element 390, and outlet cavity 384 are illustrated, there may be more than one of any of these elements, and any of these elements may have any other suitable size and shape. And although only two, straight outlet ports 386 are illustrated, each having a rectangular cross-sectional configuration, there may be fewer or more outlet ports 386, each outlet port 386 may have any other suitable size and shape, and each outlet port 386 may follow any suitable path, whether or not that path is straight. For example, there may be an array of filter mounting lips 383, filter elements 390, and outlet cavities 384; each communicating, directly or indirectly, with at least one inlet port 388 and at least one outlet port 386. The filter element 390's edges may be held in place by being sandwiched between the filter mounting lip 382 and the membrane 36. In such a case, the depth of the filter mounting lip 382 may be selected to be about the same as the thickness of the filter element 390's edges. An adhesive 394, which is compatible with the medication 12, may be used to help hold the filter element 390's edges in place between the filter mounting lip 382 and the membrane 36; and to provide a seal between the filter mounting lip 382, the filter element 390's edges, and the membrane 36. In such a case, the depth of the filter mounting lip 382 may be selected to be greater than the thickness of the filter element 390's edges, in order to provide room for the adhesive 394. The seal between the filter mounting lip 382, the filter element 390's edges, and the membrane 36 may help to prevent any leakage of the unfiltered medication 12 around the filter element 390's edges, and into the outlet cavity 384. However, such a seal may not be needed if the tolerances of the filter 380 are such that the largest gap between the filter mounting lip 382, the filter element 390's edges, and the membrane 36 is smaller than the smallest particle in the medication 12 which the filter 380 is designed to filter out of the medication 12. Alternatively, the filter mounting lip 382 may be eliminated and the filter element 390's edges may be mounted either on top of, or under, the membrane 36 by any suitable means, such as by using any suitable adhesive or bonding process. The outlet cavity 384 may be provided with at least one filter element support (not illustrated, for clarity) . The functions of each filter element support may include helping to prevent those portions of the filter element 390 which lie over the outlet cavity 384 from collapsing down into the outlet cavity 384, while simultaneously not unduly interfering with the flow of the medication 12 through the outlet cavity 384 to the outlet ports 386. Each filter element support may have any suitable size and shape. By way of example, the filter 380 may have the following physical parameters. The substrate 34 may be manufactured from 7740 Pyrex glass, may be a square having sides with a length of about 0.635 cm, and may have a maximum thickness of about 1.0 mm. The filter mounting lip 382 may have a length of about 4.6 mm; a width of about 1.8 mm; and a depth of about 65 microns, as measured from the substrate 34's top surface 46. The outlet cavity may have a length of about 4.0 mm; a width of about 1.5 mm; and a depth of about 25 microns, as measured from the substrate 34's top surface 46. The outlet ports 386 may have a length of about 3.0 mm; a width of about 250 microns; and a depth of about 25 microns, as measured from the substrate 34's top surface 46. The filter element 390 may be made from Anopore inorganic membrane having a maximum pore size of about 0.1 microns, (the Anopore inorganic membrane is described in more detail below) . The filter element 390 may have a filter area about 1.5 mm wide and about 4.0 mm long. The membrane 36 may be made from silicon, and may have a thickness of about 25 microns. When the medication 12 is distilled water, the example filter 380, having the physical parameters set forth, may have a flow rate of about 1.0 cc/day, with a pressure drop across the filter element 290 of about 5.15 mm Hg. MICROMACHINED SLAB FILTER 380 (FIGS. 14 - 16): OPERATION AND THEORY The chip 342, with its filter 380 and regulator 32, may be installed in its desired location of intended use in any suitable way. Any suitable medication supply means may be used to connect the filter 380's inlet port 388 to a source of the medication 12; and any suitable medication delivery means may be used to connect the regulator 32's outlet port 54 to whatever person, animal or thing is to receive the medication 12 from the outlet port 54. The medication supply means may also be used to supply the medication 12 to the flexure 28's top surface 62, at a pressure which may or may not be the same as the pressure at which the medication 12 is supplied to the inlet port 388. For example, the chip 342 may be installed within any type of reservoir means for the medication 12 by any suitable means, such as by locating the regulator 32's outlet port 54 over the reservoir means's outlet, and by using an adhesive face seal between the substrate 34's bottom surface 56 and the inside of the reservoir means to hold the chip 342 in place. As a result, when the reservoir means is filled with the medication 12, the chip 342 will be immersed in the medication 12, with the filter 380's inlet port 388 and the flexure 28's top surface 62 in fluid communication with the medication 12 within the reservoir means, and with the regulator 32*s outlet port 54 in fluid communication with the reservoir means' outlet. Such an installation for the chip 342 has numerous advantages. For example, it is quick, easy, reliable and inexpensive, because no additional medication supply means (such as supply conduits) are needed to supply the medication 12 to the filter 380's inlet port 388 and to the flexure 28's top surface 62 (since they are already immersed in the medication 12) ; and because no additional medication delivery means (such as delivery conduits) are needed to convey the medication 12 away from the regulator 32's outlet port 54 (since the reservoir means' outlet is used for this purpose) . Such additional inlet and outlet conduits may be undesirable since it may be relatively time consuming, difficult and expensive to align and connect them to the chip 342, due to the extremely small size of the filter 380's inlet port 388, the flexure 28, and the regulator 32's outlet port 54. Such additional inlet conduits may also be undesirable because they may tend to trap a bubble when being filled with a liquid medication 12, which bubble might then be carried into the filter 380 and the regulator 32 and cause them to malfunction. Alternatively, if the chip 342 did not have a regulator 32, but had only a filter 380, then such a chip 342 may be installed in its intended location of use in any suitable way. Any suitable medication supply means may be used to connect the filter 380's inlet port 388 to a source of the medication 12; and any suitable medication delivery means may be used to connect the filter 380's outlet ports 386 to whatever person, animal or thing is to receive the medication 12 from the outlet ports 386. The driving pressure difference (P) across the filter 380 may be defined as the driving pressure difference (P) between the flexure 28's top surface 62 and the outlet port 54. During operation, as a driving pressure difference (P) is applied across the filter 380 in any suitable way, such as by pressurizing the source of medication 12 with respect to the outlet port 54, the medication 12 will flow sequentially through the filter 380's inlet port 388, filter element 390, outlet cavity 384, and outlet ports 386. From the filter 380's outlet ports 386, the medication will then flow sequentially through the radial flow regulator 32 from its inlet ports 38 to its outlet port 54 in the manner which has been described previously regarding the radial flow regulator 32 of Figs. 1 - 2. The pore size of the filter element 390 is selected to be such that the filter element 390 will be able trap the smallest particle which the filter 380 is designed to remove from the medication 12. The pore size of the filter element 390 may depend on the size of the smallest particle which can be tolerated by the person, animal or thing which is to receive the filtered medication 12 from the filter 380. For example, if the filter 380 is intended to deliver the medication 12 to a regulator 32, as illustrated in Figs. 14 - 16, then preferably the pore size of the filter element 390 may be chosen to have a size which is at least slightly smaller than the size of the smallest fluid path dimension in the regulator 32, namely its regulator gap 48. In this way, the filter element 390 will be able to trap all of the particles in the medication 12 which might otherwise clog the smallest fluid path dimension in the regulator 32. The flow rate (Q) of the medication 12 through the filter element 390 may selected in any suitable way, such as by selectively adjusting one or more of the pertinent parameters, such as: (a) the driving pressure difference (P) across the filter 390; (b) the filter area of the filter element 390, that is the portion of the filter element 390 which is exposed to the medication 12 during use; and (c) the filter element 390's pore size. The useful life of the filter 380 is over when so many of the filter element 390's pores have been clogged by particles filtered from the medication 12 that, at the maximum desired driving pressure difference (P) across the filter 380, the minimum desired flow rate (Q) of the medication 12 through the filter 380 can no longer be achieved. Thus, both the flow rate (Q) and the useful life of the filter 380 is a function of how many of the filter element 390's pores have been clogged by particles filtered from the medication 12. For any given pore size of the filter element 390, the useful life of the filter 380 may be selectively increased or decreased, respectively, by selectively increasing or decreasing the filter area of the filter element 390. In general, it may be advantageous to provide the filter 380 with medication 12 which has been pre-filtered to a substantial degree to remove undesired particles from the medication 12 which are larger than the smallest particles which the filter 380 is intended to trap. By such pre-filtering of large particles from the medication 12, the useful life of the filter 380 may be greatly extended, since the filter 380 is a precision filter for filtering very small particles, and thus it may take only a relatively small number of large particles to clog it. The driving pressure difference (P) across the filter 380 may tend to cause portions of the filter element 390 to bow towards the outlet cavity 384's bottom surface 385. A problem may arise if any portions of the filter element 390 are forced against the cavity 384's bottom 385, since those portions of the filter element 390 would no longer be able to perform their intended filtering function. This problem may be addressed in any suitable way, such as by selectively adjusting one or more of the pertinent parameters, such as (a) the number, size, shape and location of any filter element supports for the filter element 390 which may be provided in the outlet cavity 384; (b) the size, shape and depth of the outlet cavity 384; and (c) the stiffness, elasticity, resiliency, thickness, cross-sectional configuration, size and shape of the filter element 390. The fluid resistance of the filter 380 to the medication 12 may be selectively adjusted in any suitable way, such as by selectively adjusting at least one of the pertinent parameters, such as: (a) the number, size, and shape of the inlet port 388; (b) the number, size, shape, thickness and pore size of the filter element 390; (c) the number, size, shape, and depth of the outlet cavity 384; (d) the number, size, shape and location of any filter element supports in the outlet cavity 384 for the filter element 390; and (e) the number, length, size, shape, and path followed by each of the outlet ports 386. The filter 380 may be designed to have a small, or negligible, fluid flow resistance to the medication 12 when new, in order to provide a margin for an accumulation of filtered particles in the filter element 390's pores. That is, the filter 380 may be designed so that after a predetermined quantity of particles have been trapped in the filter element 390's pores, a predetermined minimum fluid flow rate (Q) of the medication 12, at a predetermined driving pressure difference (P) across the filter 380, will still be permitted to flow through the filter 380. If this is done, and if the filter 380 is used in conjunction with a radial flow regulator 32, such as is seen in Figs. 14 - 16, then any fluid flow resistance of the medication 12 within the radial flow regulator 32 which is needed for proper pressure bias of the regulator portion 58 of the regulator 32's membrane 36, may be provided by the regulator 32's inlet ports 38 or inlet cavity 40. Alternatively, the fluid flow resistance of the filter 380 may be selected to have a significant fluid flow resistance to the medication 12 when new, in order to provide for proper pressure bias of the regulator portion 58 of the regulator 32's membrane 36. In other words, such a filter 380 may provide the dual functions of: (a) filtering out undesired particles from the medication 12; and (b) defining the flow rate operating point of the radial flow regulator 32, that is, defining the maximum flow rate (Q) of the medication 12 through the radial flow regulator 32. In this case, the flow of the medication 12 through the filter 380 may fall as the filter element 390's pores become clogged with filtered particles during use, and it may be prudent to provide some level of the pre- filtering for the medication 12 which was discussed above. MICROMACHINED SLAB FILTER 380 (FIGS. 14 - 16): MANUFACTURE The substrate 34 may be manufactured from any suitable strong, durable material which is compatible with the medication 12; in which the filter 380's mounting lip 382, outlet cavity 384, filter element supports (if any), and outlet ports 386 may be manufactured in any suitable way; and in which the regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54 may be manufactured in any suitable way. Suitable ways may include using any suitable etching, molding, stamping and machining process. Such a machining process may include the use of physical tools, such as a drill; the use of electromagnetic energy, such as a laser; and the use of a water jet. The membrane 36 may be manufactured from any suitable strong, durable, flexible, material which is compatible with the medication 12, and in which the inlet port 388 may be manufactured in any suitable way, such as by using any suitable etching, molding, stamping and machining process. Such a machining process may include the use of physical tools, such as a drill or saw; the use of electromagnetic energy, such as a laser; and the use of a water jet. The filter element 390 may be manufactured from any suitable strong, durable material which is compatible with the medication 12, which will permit the desired flow rate (Q) of the medication 12, which can withstand the desired driving pressure (P) across the filter 380, which has a pore size smaller than the smallest particle which is desired to be filtered from the medication 12, and which will not generate particles which may contaminate the medication 12. The filter element 390 may be designed to filter out any particular size of particle from the medication 12, depending on the intended use of the filter 380. If the filter 380 and the regulator 32 are intended to regulate a medication 12 which is to be supplied to a human or an animal, then any part of the filter 380 and the regulator 32 which is exposed to the medication 12 should be manufactured from, and assembled or bonded with, non¬ toxic materials. Alternatively, any toxic material which is used to manufacture the filter 380 and the regulator 32, and which is exposed to the medication 12 during use of the filter 380 and the regulator 32, may be provided with any suitable non-toxic coating which is compatible with the medication 12. Suitable materials for the substrate 34 and the membrane 36 may be metals (such as titanium) , glasses, ceramics, plastics, polymers (such as polyimides) , elements (such as silicon) , various chemical compounds (such as sapphire, and mica), and various composite materials. Suitable materials for the filter element 390 may be any suitable organic material having suitably sized pores in it, such as a thin polymer which has pores generated in it by using nuclear particle bombardment. Such a filter element 390 may be Nuclepore material made by the Nuclepore Corporation of Pleasanton, California, which may have a maximum pore size selected to be in the 0.03 to 12.0 micron range. Alternatively, the filter element 390 may be manufactured from any suitable inorganic material, such as glass, ceramic or metal which has suitably sized pores in it. For example, the filter element 390 may be made from electrolytically etched aluminum. Such a filter element 390 may be Anopore inorganic membrane, made by Whatman, Inc. of Clifton, N.J., which may have a maximum pore size selected to be in the 0.02 to 0.2 micron range. Alternatively The filter 380's membrane 36 may be manufactured from the same materials which were used to manufacture the membrane 36. The substrate 34, the membrane 36 and the filter element 390 may be assembled together in any suitable leak- proof way. Alternatively, the substrate 34, the membrane 36, and the filter element 390 may be bonded together in any suitable leak-proof way, such as by anodically bonding them together; such as by fusing them together (as by the use of heat or ultrasonic welding) ; and such as by using any suitable bonding materials, such as adhesive, glue, epoxy, solvents, glass solder, and metal solder. The substrate 34 and the membrane 36 may not necessarily be assembled or bonded together with each other in the same way in which the substrate 34, the membrane 36 and the filter element 390 are assembled or bonded together with each other. Anodically bonding the substrate 34, the membrane 36 and the filter element 390 together may be preferable for at least four reasons; which reasons are the same as, or at least similar to the reasons discussed previously regarding anodically bonding together the substrate 34 and the membrane 36 of the regulator 32 of Figs. 1 - 2. One example of how the chip 342, with its filter 380 and regulator 32, may be manufactured will now be given. The starting point may be a 76.2 mm diameter wafer of Corning 7740 Pyrex glass, which will form the substrate 34. The filter 380's mounting lip 382, outlet cavity 384, filter element supports (if any) , and outlet ports 386; and the Figs. 14 - 16 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42 and outlet cavity 52 may be manufactured in the substrate 34 in any suitable way. One suitable way may be to use an etching process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42 and outlet cavity 52, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The Figs. 14 - 16 outlet port 54 may then be manufactured in the substrate 34 in any suitable way. One suitable way may be use a laser drilling process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. A layer of corrosion-resistant material(s) may then be applied to all of the surfaces of the filter 340's mounting lip 382, outlet cavity 384, filter element supports (if any), and outlet ports 386; and to all of the surfaces of the Figs. 14 - 16 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54 in any suitable way. One suitable way may be to use an application process which is the same as, or at least similar to, that used to apply a layer of corrosion- resistant material(s) to the Figs. 1 - 2 regulator 32's inlet channels 38, inlet cavity 40, regulator seat 42, outlet cavity 52, and outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The filter element 390 then be placed on the substrate 34 with its edges being supported by the filter mounting lip 382 and with its central portions being supported by the filter element supports (if any) . The membrane 36, with its inlet port 388, may be manufactured from a silicon wafer, and secured to the glass wafer (which is the substrate 34) in any suitable way. The structure, operation, theory and manufacture of the filter 380's membrane 36, with its inlet port 388, the securing of the membrane 36 to its substrate 34 is the same as, or at least similar to, the manufacturing of the linear flow regulator 80's membrane 84, with its inlet port 88, and the securing of its membrane 84 to its substrate 86, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. It may be preferred that the filter element 390 be made from an inorganic membrane, such as the etched aluminum membrane which was described above, if the filter 380's substrate 34 and membrane 36 are bonded together by using a high temperature process, such as the anodic bonding process which was described above regarding the Figs. 1 - 2 regulator 32's substrate 34 and membrane 36. That would offer several advantages, such as allowing the filter element 390 to be simultaneously incorporated into the filter 380 during the manufacture of the regulator 32 on the chip 342; allowing the edges of the filter element 390 to be simultaneously anodically bonded to the substrate 34 and membrane 36 (thereby eliminating the need for any other bonding and sealing materials for this purpose) ; and permitting the high anodic bonding temperature, to simultaneously burn out or volatilize any organic debris which may be located within the filter 380 and regulator 32. As was mentioned above, although the filter 380 is illustrated in Figs. 14 - 16 as being manufactured on the chip 342 with a regulator 32, the filter 380 may be manufactured by itself on the chip 342, without a regulator 32. In such a case, all or part of the filter 380's outlet ports 386 may extend from the outlet cavity 384 down through the substrate 34 (in a fashion similar to the regulator 32's outlet port 54). Such downwardly extending outlet ports 386 for the filter 380 may have any suitable shape, such as a venturi shape; and may be manufactured in any suitable way. One suitable way may be use a laser drilling process which is the same as, or at least similar to, that used to manufacture the Figs. 1 - 2 regulator 32's outlet port 54, except for those differences, if any, which will be made apparent by an examination of all of the Figures and disclosures in this document. The manufacture of only one filter 380, and the manufacture of only one filter 380/regulator 32 combination were described above. However, it will be appreciated that on any pair of glass and silicon wafers the substrates 34 and the membranes 36 for a large number of filters 380, or filter 380/regulator 32 combinations could be manufactured simultaneously in a manner similar to that described above. If such is the case, an array of substrates 34 may be simultaneously etched in the glass wafer; their outlet ports 54 may be drilled, and the layer of one or more corrosion-resistant substances may be applied to the substrates 34. Then an array of inlet ports 288 may be simultaneously etched in the silicon wafer. Then the silicon and glass wafers for the substrates 34 and the membranes 36 may be aligned and secured together. Then, all of the membranes 36 may be manufactured simultaneously by grinding and etching the silicon wafer to its desired final thickness. The silicon/glass substrate 34/membrane 36 sandwich may then be divided by any suitable means (such as dicing) into individual chips, each chip bearing at least one filter 380 or filter 380/regulator 32 combination. One of the advantages of using etching and anodic bonding processes to manufacture the filter 380, and the filter 380/regulator 32 combination, is that such processes enable high quality, very reliable filters 380, and filter 380/regulator 32 combinations, to be mass produced in great numbers at a cost so low that the filters 380 and the filter 380/regulator 32 combinations may be considered to be disposable. Further, it should also be noted that the filter 380 and the filter 380/regulator 32 combination are stunning in their simplicity since they both have only two basic parts, i.e. their substrates 34 and their membranes 36; and since the regulator 32 has only one moving part, i.e., its flexure 28, which merely bows during operation of the filter 380/regulator 32 combination. In addition, because the raw materials from which the filter 380 and the filter 380/regulator 32 combination may be manufactured may be very inexpensive, such as glass and silicon, the cost of the filter 380 and the filter 380/regulator 32 combination may held to a very low level. MICROMACHINED SLAB FILTER 400 (FIG. 17): STRUCTURE, OPERATION, THEORY AND MANUFACTURE The micromachined slab filter 400 which is illustrated in Fig. 17 is the same as, or at least similar to, the micromachined slab filter 340 of Figs. 14 - 16 in its structure, operation, theory and manufacture, except for those differences which will be made apparent by an examination of all of the Figures and all of the disclosures in this document. Accordingly, the respective parts of the filter 400 of Fig. 17 has been given the same reference numerals as the corresponding parts of the filter 340 of Figs. 14 - 16, for clarity and simplicity. Turning again to Fig. 17, it is seen that the substrate 34 may be provided with a filter element entrance 402, which may extend from the filter mounting lip 382 to the edge of the substrate 34. The filter element entrance 402 and the filter mounting lip 382 may be recessed below the substrate 34's top surface by about the same amount. As a result, after the slab filter 400's substrate 34 and membrane 36 are bonded together, the filter element entrance 402 and the overlaying portion of the membrane 36 form a slot through which the filter element 390 may be inserted into position on the filter mounting lip 382. After the filter element 390 is in place on the filter mounting lip 382, the filter element may be bonded and sealed in place in any suitable way, such as by using a bonding and sealing process which is the same as, or at least similar to, the bonding and sealing process which was used to bond and seal the Figs. 14 - 16 substrate 34, filter element 390 and membrane 36 together, except for those differences which will be made apparent by an examination of all of the Figures and disclosures in this document. It is understood that the foregoing forms of the invention were described and/or illustrated strictly by way of non-limiting example. In view of all of the disclosures herein, these and further modifications, adaptations and variations of the present invention will now be apparent to those skilled in the art to which it pertains, within the scope of the following claims.

Claims: What is claimed is: 1. A micromachined fluid handling apparatus, wherein said apparatus comprises a micromachined filter, and a micromachined fluid handling device; wherein said fluid handling apparatus comprises a substrate and a membrane; wherein said substrate comprises a mounting portion; wherein said membrane comprises a mounting portion; wherein said substrate's and said membrane's mounting portions are secured together; wherein said filter and said fluid handling device also comprise said substrate and said membrane; wherein said filter further comprises a filter element means for removing particles of at least a predetermined size from an unfiltered fluid from an unfiltered fluid source, a first inlet port means for receiving said unfiltered fluid from said unfiltered fluid source and for conveying said unfiltered fluid to said filter element means, and a first outlet port means for conveying a filtered fluid from said filter element means and for permitting said filtered fluid to exit from said filter; wherein said fluid handling device comprises a second inlet port means for receiving said filtered fluid from said first outlet port means, and a second outlet port means for permitting said filtered fluid to exit from said fluid handling device. 2. The apparatus according to claim 1, wherein said substrate's and membrane's mounting portions are anodically bonded to each other. 3. The apparatus according to claim 1, wherein said apparatus comprises at least one exposed portion which is exposed to said fluid during operation of said apparatus; wherein said apparatus further comprises a corrosion- resistant layer on at least part of said exposed portion; and wherein said corrosion-resistant layer is anodically bonded to said exposed portion. 4. The apparatus according to claim 3, wherein said corrosion-resistant layer comprises an oxide of a transition metal selected from the group consisting essentially of titanium and zirconium. 5. The apparatus according to claim 3, wherein said corrosion-resistant layer serves the dual functions of helping to prevent corrosion of said exposed portion of said apparatus, and helping to prevent said exposed portion of said apparatus from being anodically bonded to said membrane. 6. The apparatus according to claim 1, wherein said filter element means comprises an array of filter slots micromachined into said substrate. 7. The apparatus according to claim 6, wherein said array of filter slots at least substantially surrounds said fluid handling device. 8. The apparatus according to claim 7, wherein said fluid handling device comprises a radial flow regulator; and wherein said radial flow regulator further comprises a regulator seat micromachined into said substrate; a flexure portion of said membrane which extends over said regulator seat, wherein said flexure has a top surface and a bottom surface; and a regulator gap located between said flexure's bottom surface and said regulator seat; wherein said second inlet port means are also for conveying said filtered fluid to said regulator gap; wherein said second outlet port means are also for conveying said filtered fluid from said regulator gap; wherein, during operation of said regulator, said flexure's top surface is exposed to said unfiltered fluid from said unfiltered fluid source; wherein there is a driving pressure difference of said unfiltered fluid between said first inlet port means and said second outlet port means; wherein said driving pressure difference also acts between said flexure's top surface and said second outlet port means; wherein, in response to an increase in said driving pressure difference, said flexure bows towards said regulator seat an increased amount, to reduce the size of said regulator gap and to tend to hold a flow of said filtered fluid through said regulator within a predetermined fluid flow range, despite said increase in said driving pressure difference; and wherein, in response to a decrease in said driving pressure difference, said flexure bows towards said regulator seat a decreased amount, to increase the size of said regulator gap and to tend to hold said flow of said filtered fluid through said regulator within said predetermined fluid flow range, despite said decrease in said driving pressure difference. 9. The apparatus according to claim 7, wherein said first inlet port means comprises an inlet cavity for distributing said unfiltered fluid to said array of filter slots; wherein said inlet cavity at least substantially surrounds said array of filter slots; wherein said first outlet port means comprises an outlet cavity for collecting said filtered fluid from said array of filter slots; and wherein said outlet cavity at least substantially surrounds said fluid handling device. 10. The apparatus according to claim 9, wherein said fluid handling device comprises a radial flow regulator; and wherein said radial flow regulator further comprises a regulator seat micromachined into said substrate; a flexure portion of said membrane which extends over said regulator seat, wherein said flexure has a top surface and a bottom surface; and a regulator gap located between said flexure's bottom surface and said regulator seat; wherein said second inlet port means are also for conveying said filtered fluid to said regulator gap; wherein said second outlet port means are also for conveying said filtered fluid from said regulator gap; wherein, during operation of said regulator, said flexure's top surface is exposed to said unfiltered fluid from said unfiltered fluid source; wherein there is a driving pressure difference of said unfiltered fluid between said first inlet port means and said second outlet port means; wherein said driving pressure difference also acts between said flexure's top surface and said second outlet port means; wherein, in response to an increase in said driving pressure difference, said flexure bows towards said regulator seat an increased amount, to reduce the size of said regulator gap and to tend to hold a flow of said filtered fluid through said regulator within a predetermined fluid flow range, despite said increase in said driving pressure difference; and wherein, in response to a decrease in said driving pressure difference, said flexure bows towards said regulator seat a decreased amount, to increase the size of said regulator gap and to tend to hold said flow of said filtered fluid through said regulator within said predetermined fluid flow range, despite said decrease in said driving pressure difference. 11. The apparatus according to claim 1, wherein said filter element means comprises a slab filter element; wherein said first inlet port means comprises an inlet port in said membrane; wherein said first outlet port means comprises an outlet cavity in said substrate; and wherein, during operation of said filter, said unfiltered fluid flows from said membrane's inlet port to said slab filter element, and wherein said filtered fluid flows from said slab filter element to said substrate's outlet cavity. 12. The apparatus according to claim 11, wherein said fluid handling device comprises a radial flow regulator; and wherein said radial flow regulator further comprises a regulator seat micromachined into said substrate; a flexure portion of said membrane which extends over said regulator seat, wherein said flexure has a top surface and a bottom surface; and a regulator gap located between said flexure's bottom surface and said regulator seat; wherein said second inlet port means are also for conveying said filtered fluid to said regulator gap; wherein said second outlet port means are also for conveying said filtered fluid from said regulator gap; wherein, during operation of said regulator, said flexure's top surface is exposed to said unfiltered fluid from said unfiltered fluid source; wherein there is a driving pressure difference of said unfiltered fluid between said first inlet port means and said second outlet port means; wherein said driving pressure difference also acts between said flexure's top surface and said second outlet port means; wherein, in response to an increase in said driving pressure difference, said flexure bows towards said regulator seat an increased amount, to reduce the size of said regulator gap and to tend to hold a flow of said filtered fluid through said regulator within a predetermined fluid flow range, despite said increase in said driving pressure difference; and wherein, in response to a decrease in said driving pressure difference, said flexure bows towards said regulator seat a decreased amount, to increase the size of said regulator gap and to tend to hold said flow of said filtered fluid through said regulator within said predetermined fluid flow range, despite said decrease in said driving pressure difference. 13. The apparatus according to claim 11, wherein said filter element is located between said membrane's inlet port and said substrate's outlet cavity. 14. The apparatus according to claim 11, wherein said filter further comprises a filter element entrance means for permitting said filter element to be inserted between said membrane's inlet port and said substrate's outlet cavity. 15. The apparatus according to claim 11, wherein said filter element comprises an exposed filter element area which is exposed to said unfiltered fluid; wherein said membrane's inlet port has an area which is at least about equal to said exposed filter element area; and wherein said substrate's outlet cavity has an area which is at least about equal to said exposed filter element area. 16. The apparatus according to claim 1, wherein said filter element means comprises a slab filter element; wherein said first inlet port means comprises a surface of said slab filter element which is exposed to said unfiltered fluid during use of said filter; wherein said first outlet port means comprises an outlet port in said membrane and an outlet cavity in said substrate; wherein said membrane is located between said filter element means and said substrate; and wherein, during operation of said filter, said filtered fluid flows sequentially through said membrane's outlet port and said substrate's outlet cavity. 17. A micromachined filter comprising a substrate, a membrane, and a filter element means for removing particles of at least a predetermined size from an unfiltered fluid from an unfiltered fluid source; wherein said substrate comprises a mounting portion; wherein said membrane comprises a mounting portion; wherein said substrate's and said membrane's mounting portions are secured together; wherein said filter further comprises an inlet port means for receiving said unfiltered fluid from said unfiltered fluid source, and for conveying said unfiltered fluid to said filter element means; and an outlet port means for conveying a filtered fluid from said filter element means and for permitting said filtered fluid to exit from said filter. 18. The filter according to claim 17, wherein said substrate's and membrane's mounting portions are anodically bonded to each other. 19. The filter according to claim 17, wherein said filter comprises at least one exposed portion which is exposed to said fluid during operation of said apparatus; wherein said apparatus further comprises a corrosion- resistant layer on at least part of said exposed portion; and wherein said corrosion-resistant layer is anodically bonded to said exposed portion. 20. The filter according to claim 19, wherein said corrosion-resistant layer comprises an oxide of a transition metal selected from the group consisting essentially of titanium and zirconium. 21. The filter according to claim 19, wherein said corrosion-resistant layer serves the dual functions of helping to prevent corrosion of said exposed portion of said apparatus, and helping to prevent said exposed portion of said apparatus from being anodically bonded to said membrane. 22. The filter according to claim 17, wherein said filter element means comprises an array of filter slots micromachined into said substrate. 23. The filter according to claim 22, wherein said array of filter slots form an at least substantially closed figure. 24. The filter according to claim 23, wherein said inlet port means comprises an inlet cavity for distributing said unfiltered fluid to said array of filter slots; wherein said inlet cavity at least substantially surrounds said array of filter slots; wherein said outlet port means comprises an outlet cavity for collecting said filtered fluid from said array of filter slots; and wherein said array of filter slots at least substantially surrounds said outlet cavity. 25. The filter according to claim 17, wherein said filter element means comprises a slab filter element; wherein said inlet port means comprises an inlet port in said membrane; wherein said outlet port means comprises an outlet cavity in said substrate; and wherein, during operation of said filter, said unfiltered fluid flows from said membrane's inlet port to said slab filter element, and wherein said filtered fluid flows from said slab filter element to said substrate's outlet cavity. 26. The filter according to claim 25, wherein said filter element is located between said membrane's inlet port and said substrate's outlet cavity. 27. The filter according to claim 26, wherein said filter further comprises a filter element entrance means for permitting said filter element to be inserted between said membrane's inlet port and said substrate's outlet cavity. 28. The filter according to claim 25, wherein said filter element comprises an exposed filter element area which is exposed to said unfiltered fluid; wherein said membrane's inlet port has an area which is at least about equal to said exposed filter element area; and wherein said substrate's outlet cavity has an area which is at least about equal to said exposed filter element area. 29. The filter according to claim 25, wherein said filter element means comprises a slab filter element; wherein said inlet port means comprises a surface of said slab filter element which is exposed to said unfiltered fluid during use of said filter; wherein said outlet port means comprises an outlet port in said membrane and an outlet cavity in said substrate; wherein said membrane is located between said filter element means and said substrate; and wherein, during operation of said filter, said filtered fluid flows sequentially through said membrane's outlet port and said substrate's outlet cavity. 30. A method for manufacturing a micromachined fluid handling apparatus, wherein said apparatus comprises a micromachined filter, and a micromachined fluid handling device; wherein said fluid handling apparatus comprises a substrate and a membrane; wherein said substrate comprises a mounting portion; wherein said membrane comprises a mounting portion; wherein said filter and said fluid handling device also comprise said substrate and said membrane; wherein said filter further comprises a filter element means for removing particles of at least a predetermined size from an unfiltered fluid from an unfiltered fluid source, a first inlet port means for receiving said unfiltered fluid from said unfiltered fluid source and for conveying said unfiltered fluid to said filter element means, and a first outlet port means for conveying a filtered fluid from said filter element means and for permitting said filtered fluid to exit from said filter; wherein said fluid handling device comprises a second inlet port means for receiving said filtered fluid from said first outlet port means, and a second outlet port means for permitting said filtered fluid to exit from said fluid handling device; and wherein said method comprises the steps of: micromachining at least a portion of at least one of said filter means and said fluid handling device by etching at least a portion of said filter means and said fluid handling device into said substrate; and securing said membrane's and substrate's mounting portions together. 31. The method according to claim 30, wherein said method further comprises micromachining at least a portion of both said filter means and said fluid handling device by etching at least a portion of both said filter means and said fluid handling device into said substrate. 32. The method according to claim 30, wherein said filter element means comprises an array of filter slots micromachined into said substrate; and wherein said method further comprises the step of micromachining at least a portion of said array of filter slots into said substrate. by etching at least a portion of said array of filter slots into said substrate prior to performing said securing step. 33. The method according to claim 32, wherein said first inlet port means comprises an inlet cavity in said substrate for distributing said unfiltered fluid to said array of filter slots; and wherein said method further comprises the step of micromachining at least a portion of said inlet cavity into said substrate, by etching at least a portion of said inlet cavity into said substrate prior to performing said securing step. 34. The method according to claim 32, wherein said first outlet port means comprises an outlet cavity in said substrate for collecting said filtered fluid from said array of filter slots; and wherein said method further comprises the step of micromachining at least a portion of said outlet cavity into said substrate, by etching at least a portion of said outlet cavity into said substrate prior to performing said securing step. 35. The method according to claim 30, wherein said filter element means comprises a slab filter element; wherein said first inlet port means comprises an inlet port in said membrane; wherein said first outlet port means comprises an outlet cavity in said substrate; wherein, during operation of said filter, said unfiltered fluid flows from said membrane's inlet port to said slab filter element, and wherein said filtered fluid flows from said slab filter element to said substrate's outlet cavity; and wherein said method further comprises the steps of micromachining at least a portion of said inlet port and said outlet cavity into said membrane and said substrate, respectively, by etching at least a portion of said inlet port and said outlet cavity into said membrane and said substrate, respectively, prior to performing said securing step. 36. The method according to claim 30, wherein said filter element means comprises a slab filter element; wherein said first inlet port means comprises a surface of said slab filter element which is exposed to said unfiltered fluid during use of said filter; wherein said first outlet port means comprises an outlet port in said membrane and an outlet cavity in said substrate; wherein said membrane is located between said filter element means and said substrate; wherein, during operation of said filter, said filtered fluid flows sequentially through said membrane's outlet port and said substrate's outlet cavity; and wherein said method further comprises the steps of micromachining at least a portion of said outlet port and said outlet cavity into said membrane and said substrate, respectively, by etching at least a portion of said outlet port and said outlet cavity into said membrane and said substrate, respectively, prior to performing said securing step. 37. The method according to claim 30, wherein said securing step comprises anodically bonding said substrate's and membrane's mounting portions together. 38. The method according to claim 30, wherein said method further comprises the steps of applying at least one layer of at least one corrosion-resistant material to at least a portion of said apparatus; and securing said layer of at least one corrosion-resistant material to said apparatus by using anodic bonding. 39. The method according to claim 38, wherein said steps of securing said substrate's and membrane's mounting ' portions together and of securing said at least one layer of at least one corrosion-resistant material to said apparatus occur simultaneously; and wherein both of said steps of securing comprise anodic bonding. 40. The method according to claim 30, wherein said method further comprises forming said membrane by the steps of providing a wafer of material having a first layer which is etchable by a first etchant, and having a second layer which is not etchable by said first etchant; wherein said second layer has a thickness about equal to the desired final thickness of said membrane; securing said second layer to said substrate during said step of securing said membrane to said substrate; and etching away at least a portion of said first layer with said first etchant. 41. The method according to claim 40, wherein said first inlet port means comprise an inlet port in said membrane; wherein both said first and second layers are etchable by a second etchant; and wherein said method further comprises micromachining said inlet port into said membrane by etching said inlet port into said wafer's second layer to a depth in excess of said desired final thickness of said membrane, prior to performing said securing step. 42. A method for manufacturing a filter comprising a substrate, a membrane, and a filter element means for removing particles of at least a predetermined size from an unfiltered fluid from an unfiltered fluid source; wherein said substrate comprises a mounting portion; wherein said membrane comprises a mounting portion; wherein said filter further comprises an inlet port means for receiving said unfiltered fluid from said unfiltered fluid source, and for conveying said unfiltered fluid to said filter element means; and an outlet port means for conveying a filtered fluid from said filter element means and for permitting said filtered fluid to exit from said filter; and wherein said method comprises the steps of: micromachining at least a portion of at least one of said inlet port means, said filter element means and said outlet port means, by etching at least a portion of at least one of said inlet port means, said filter element means and said outlet port means into said substrate; and securing said membrane's and substrate's mounting portions together. 43. The method according to claim 42, wherein said filter element means comprises an array of filter slots micromachined into said substrate; and wherein said method further comprises the step of micromachining at least a portion of said array of filter slots into said substrate, by etching at least a portion of said array of filter slots into said substrate prior to performing said securing step. 44. The method according to claim 42, wherein said inlet port means comprises an inlet cavity in said substrate for distributing said unfiltered fluid to said array of filter slots; and wherein said method further comprises the step of micromachining at least a portion of said inlet cavity into said substrate, by etching at least a portion of said inlet cavity into said substrate prior to performing said securing step. 45. The method according to claim 44, wherein said outlet port means comprises an outlet cavity in said substrate for collecting said filtered fluid from said array of filter slots; and wherein said method further comprises the step of micromachining at least a portion of said outlet cavity into said substrate, by etching at least a portion of said outlet cavity into said substrate prior to performing said securing step. 46. The method according to claim 42, wherein said filter element means comprises a slab filter element; wherein said inlet port means comprises an inlet port in said membrane; wherein said outlet port means comprises an outlet cavity in said substrate; wherein, during operation of said filter, said unfiltered fluid flows from said membrane's inlet port to said slab filter element, and wherein said filtered fluid flows from said slab filter element to said substrate's outlet cavity; and wherein said method further comprises the steps of micromachining at least a portion of said inlet port and said outlet cavity into said membrane and said substrate, respectively, by etching at least a portion of said inlet port and said outlet cavity into said membrane and said substrate, respectively, prior to performing said securing step. 47. The method according to claim 42, wherein said filter element means comprises a slab filter element; wherein said inlet port means comprises a surface of said slab filter element which is exposed to said unfiltered fluid during use of said filter; wherein said outlet port means comprises an outlet port in said membrane and an outlet cavity in said substrate; wherein said membrane is located between said filter element means and said substrate; wherein, during operation of said filter, said filtered fluid flows sequentially through said membrane's outlet port and said substrate's outlet cavity; and wherein said method further comprises the steps of micromachining at least a portion of said outlet port and said outlet cavity into said membrane and said substrate, respectively, by etching at least a portion of said outlet port and said outlet cavity into said membrane and said substrate, respectively, prior to performing said securing step. 48. The method according to claim 42, wherein said securing step comprises anodically bonding said substrate's and membrane's mounting portions together. 49. The method according to claim 43, wherein said method further comprises the steps of applying at least one layer of at least one corrosion-resistant material to at least a portion of said apparatus; and securing said layer of at least one corrosion-resistant material to said apparatus by using anodic bonding. 50. The method according to claim 49, wherein said steps of securing said substrate's and membrane's mounting portions together and of securing said at least one layer of at least one corrosion-resistant material to said apparatus occur simultaneously; and wherein both of said steps of securing comprise anodic bonding. 51. The method according to claim 42, wherein said method further comprises forming said membrane by the steps of providing a wafer of material having a first layer which is etchable by a first etchant, and having a second layer which is not etchable by said first etchant; wherein said second layer has a thickness about equal to the desired final thickness of said membrane; securing said second layer to said substrate during said step of securing said membrane to said substrate; and etching away at least a portion of said first layer with said first etchant. 52. The method according to claim 51, wherein said inlet port means comprise an inlet port in said membrane; wherein both said first and second layers are etchable by a second etchant; and wherein said method further comprises micromachining said inlet port into said membrane by etching said inlet port into said wafer's second layer to a depth in excess of said desired final thickness of said membrane, prior to performing said securing step.

Inventors: LAWRENCE DALE M, SAASKI ELRIC W, LAWRENCE, DALE, M., SAASKI, ELRIC, W.
Applicants: RES INT INC, RESEARCH INTERNATIONAL, INC.
Application year: 1994
Main classification: F15C5
IPC codes: B01D61, B01D67, B01D69, B01D71, F04B43, F15C5, F16K99, G05D7